## NO x 

## EMISSIONS STUDY

PerformedAt 

## Hibbing Taconite Company Hibbing Facility AQ Facility 10 

## Number: 13700061-002/541 AQ File Number: AQ#541 Multiple Emission Sources Hibbing, Minnesota

Emission Facility Contact Person 

## Ms. Andrea Hayden Hibbing Taconite Company Highway 5 North Hibbing, MN 55746 Telephone: (218) 262-6856 Fax: (218) 262-6877 Email: ajhayden@cleveland-cliffs.com

TestDates 

## May 1- 8, 2007

ReportNo. 

## GE Energy Management Services, Inc. Report M22A0346B Revision 1 - November 1, 2007 ReportSubmittalDate 

## May 31,2007 ISO 9001 Accredited Quality System

GE Energy Management Services, Inc. 1301 Corporate Center Drive-Suite 177 Eagan, MN 55121 USA T (651) 686-0700 F (651) 686-4434

# GE Energy

NOx 

## EMISSIONS STUDY

PerformedAt 

## Hibbing Taconite Hibbing Faciity Multiple Emission Sources Hibbing, Minnesota
Test Dates 

## May 1- 

## 8, 2007 James Tryba Senior Project Manager

ISO 9001 Accredited Quality System



### ReportNo. 

## GE Energy Management Services, Inc. Report M22A03468 Revision 1 - November 1, 2007

ReportSubmittalDate 

## May 31,2007

GE Energy Management Services, Inc. 1301 Corporate Center Drive-Suite 177 Eagan, MN 55121 USA



# • T (651) 686-0700 F (651) 686-4434

# , I GE Energy

I ael Anderson

Date Printed Name of Person 5-31-2007 

### o a that the sampling procedures were performed in accordance with the e data presented in this test report are, to the best of my knowledge and plete. All exceptions are listed and explained below." 1. Certification of sampling procedures by the team leader ofthe personnel conducting the sampling procedures: 

### "I certify under penalty approved test plan and belief, true, accurate, a .?



### 2. Certification of analytical procedures by the person responsible for the laboratoryanalysis offield samples: 

### "I certify under penalty of law that the analytical procedures were performed in accordance with the requirements of the test methods and that the data presented for use in the test report were, to the best of my knowledge and belief, true, accurate, and complete. All exceptions are listed and explained below." 

## CERTIFICATIONS REQUIRED FOR PERFORMANCE TEST REPORTS M22A0346B 

# I I I I I 

# , I I Not Applicable Signature: 

### Title Printed Name of Person
Date 

# I I 

# I James Tryba Printed Name of Person 5-31-2007 Date 

# I I I 

# I I 4. Certification of test report by owner or operator of the emission facility: 

### "I certify under penalty of law that the information submitted in this test report accurately reflects the operating conditions at the emission facility during this performance test and describes the date and nature of all operational and maintenance activities that were performed on process and control equipment during the month prior to the performance test. Based on my inquiry of the person or persons who performed the operational and maintenance activities, the information submitted in this test report is, to the best of my knowledge and**bel'~'ef'** 

### true accurate, and complete. All exceptions are listed and explained below."

< 

# :AndreA.'""X 

# H@j.deVl Signature:

. Printed Name of Person

# Till~VI VQVJ Wlc:'ia¥ 

# I

# ~,.:h,1yJ M"

# V1tU'(=C**---=-Da-:-te-l,,(Q~/1-+7-f!-LDL7+-.** -----------

@ 2007, General Electric Company. All rights reserved. The contents of this document are the property of General Electric Company. No part of this work may be reproduced or transmitted in any form or by any means, except as permitted in written license agreement with General Electric Company. General Electric Company has made every reasonable attempt to ensure the completeness and accuracy of this document. The GE logo is a registered trademarkof General Electric Company. 

# I

# GE Energy

TABLE OF CONTENTS

CERTIFICATIONS REQUIRED FOR PERFORMANCE TEST REPORTS 

## i 1.0 INTRODUCTION 

## 1 2.0 SUMMARYAND DISCUSSION OF RESULTS 

## 2 3.0 EMISSION UNIT OPERATING PARAMETERS AND MAINTENANCE 

## 3 4.0 SAMPLING AND ANALYSIS PROCEDURES 

## 4 4.1 Description of Sampling Location 

## 4 4.2 Volumetric Flow Rate Determination by USEPA Method 

## 2 4 4.3 CO2 

### and O2 

### Determination by USEPA Method 3 4 

## 4.4 Determination of the Concentration of Gaseous Pollutants Using the Multi-Pollutant Sampling System 5 

## 4.4.1 NOx 

### Determination by USEPA Method 7E 5 4.5 Moisture Determination by USEPA Method 4 5 

## 5.0 QUALITYASSURANCE PROCEDURES 6 

## 6.0 TEST RESULTS SUMMARy 7

APPENDIX Project Participants 

## 21 Process and Air Pollution Control Equipment Operating Data 

## 22 Test Section Diagrams 31 Sample Train Diagrams 

## 32 Calculation Nomenclature and Formulas 35 Test Data and Results 38 Field Data Sheets 98 Calibration Data 

## 180 N02 Converter Efficiency Data 

## 182 Calibration Gas Certificates 183 Test Plan and Approval Letter 

## 188

# GE Energy

NOx 

## EMISSIONS STUDY Performed At Hibbing Taconite

Hibbing Faciity Multiple Emission Sources Hibbing, Minnesota May 1- 8, 2007

1.0 INTRODUCTION GE Energy Management Services, Inc., ("GE Energy") performed an emission test program at the Hibbing Faciity of Hibbing Taconite in Hibbing, Minnesota on May 1-8, 2007. The tests were authorized by and performed for Hibbing Taconite. The purpose of this test program was to quantify emissions of nitrogen oxides (NOx) 

## from the emissions sources identified in the following table:

StackVent Control Emission Emission Unit 

## I Control Equipment Title V Equipment Group 

## 1.0. 1.0. Unit 

## 1.0. Description No.

SV021 CE022 EU020 Pellet Furnace Line 1 / Venturi Scrubber GPOO3 SV022 CE023 EU020 Pellet Furnace Line 1 / Venturi Scrubber GPOO3 SV023 CE024 EU020 Pellet Furnace Line 1 / Venturi Scrubber GPOO3 SV024 CE025 EU020 Pellet Furnace Line 1 / Venturi Scrubber GPOO3 SV025 CE027 EU021 Pellet Furnace Line 2 / Venturi Scrubber GPOO3 SV026 CE028 EU021 Pellet Furnace Line 2 / Venturi Scrubber GPOO3 SV027 CE029 EU021 Pellet Furnace Line 2 / Venturi Scrubber GPOO3 SV028 CE030 EU021 Pellet Furnace Line 2 / Venturi Scrubber GPOO3 SV029 CE032 EU022 Pellet Furnace Line 3 / Venturi Scrubber GPOO3 SV030 CE033 EU022 Pellet Furnace Line 3 /Venturi Scrubber GPOO3 SV031 CE034 EU022 Pellet Furnace Line 3 / Venturi Scrubber GPOO3 SV032 CE035 EU022 Pellet Furnace Line 3/Venturi Scrubber GPOO3 

## The tests were performed to quantify NOx emissions for the Air Emission Inventories for the years 2007 through 2011. The MPCA declined to observe the tests.

GE EnergyProject M22A0346BRev.1 

# 1

# GE Energy

2.0 SUMMARY AND DISCUSSION OF RESULTS The following tables present the measured emission of each pollutant of concern. Detailed individual run results are presented in Section 6.0.

Stack Control Emission Unit Average NOx Average NOx Vent I.D. Equipment I.D. Concentration Emission Rate I.D. (ppm) (Ib/hr)

SV021 CE022 EU020 33.2 42.10 SV022 CE023 EU020 60.5 74.36 SV023 CE024 EU020 94.0 86.76 SV024 CE025 EU020 100.7 112.96 SV025 CE027 EU021 109.3 114.83 SV026 CE028 EU021 103.5 119.33 SV027 CE029 EU021 68.1 79.35 SV028 CE030 EU021 52.9 66.25 SV029 CE032 EU022 32.3 40.98 SV030 CE033 EU022 47.5 59.43 SV031 CE034 EU022 68.8 83.04 SV032 CE035 EU022 100.3 120.99



## Average NOx Furnace Line No. Emission Unit I.D. StackVent I.D. Emission Rate (lb/MMBtu)

SV021 1 EU020 SV022 3.63 SV023 SV024 SV025 2 EU021 SV026 3.75 SV027 SV028 SV029 3 EU022 SV030 2.92 SV031 SV032

GE Energy Project M22A0346B Rev.1 

# 2

# GE Energy

No problems were encountered with the testing equipment during the test program. The results presented in this report contain no known errors. The following table presents a summary of relevant process and/or Air Pollution Control Equipment (APCE) operating data.
Average Wet Scrubber Parameters

StackVent I.D. Control Average Process Rate (APCE) Equipment I.D. Pressure Drop WaterFlow (in. w.e.) (gpm)
SV021 CE022 371 

### dry long tons/hr Demist Panel - 0.48 1051 Venturi - 3.50 SV022 CE023 372 

### dry long tons/hr Demist Panel- 0.41 1025 Venturi - 5.06 SV023 CE024 369 

### dry long tons/hr Demist Panel- 0.55 1073 Venturi - 3.78 SV024 CE025 363 

### dry long tons/hr Demist Panel - 0.32 661 Venturi - 4.29 SV025 CE027 292 

### dry long tons/hr Demist Panel- 1.08 387 Venturi - 4.63 SV026 CE028 361 

### dry long tons/hr Demist Panel - 0.87 985 Venturi - 4.79 SV027 CE029 368 

### dry long tons/hr Demist Panel - 0.39 894 Venturi - 5.31 SV028 CE030 368 

### dry long tons/hr Dernist Panel- 0.55 966 Venturi - 3.98 SV029 CE032 374 

### dry long tons/hr Demist Panel - 0.35 690 Venturi - 4.99 SV030 CE033 369 

### dry long tons/hr Demist Panel - 0.28 731 Venturi - 4.02 SV031 CE034 370 

### dry long tons/hr Demist Panel - 0.32 667 Venturi - 2.89 SV032 CE035 376 

### dry long tons/hr Demist Panel - 0.22 513 Venturi - 4.33



# 3.0 EMISSION UNIT OPERATING PARAMETERS AND MAINTENANCE 

## The following information is presented in the appendix of this report: • Process and APCE operating data

GE EnergyProjectM22A0346BRev.1 

# 3

# GE Energy

4.0 SAMPLING AND ANALYSIS PROCEDURES All testing, sampling, analytical, and calibration procedures used for this test program were performed as described in the Title 40, 

## Code of Federal Regulations, Part 60 (40CFR60), Appendix A, Methods 1, 2, 3, 4, 7E and the latest revisions thereof. Where applicable, the 

## Quality Assurance Handbook for Air Pollution Measurement Systems, Volume III, Stationary Source SpecificMethods, United States Environmental Protection Agency (USEPA) 600/R94/038c, September 1994 was used to supplement procedures.
4.1 Description of Sampling Location The sample location for each emission source tested was a vertical circular duct equipped with two sample ports. The ports were installed 1.8 duct diameters upstream, and 8.6 duct diameters downstream from the nearest flow disturbance. Diagrams depicting all relevant duct dimensions are appended. The USEPA reference Method(s) used to determine the number and location of sample points is identified in the following sections.
4.2 Volumetric Flow Rate Determination by USEPA Method 2 This method is applicable for measurement of the average velocity of a gas stream and for quantifying gas flow at measurement sites that meet the criteria of Section 2.1 of USEPA Method 1, 40CFR60, Appendix A. 

## A calibrated, S-type pitot tube and inclined manometer were used to measure the velocity head**(~P)** 

## at each sample point. The temperature at each sample point was measured with a Type K thermocouple and a calibrated digital temperature indicator. The number and location of sample points was determined in accordance with USEPA Method 1. 4.3 CO2 

## and O2 

## Determination by USEPA Method 3 This method is applicable for determining C02 and O2 concentrations and dry molecular weight of a sample from a gas stream of a fossil fuel-fired process. This method may also be applicable to other processes where it has been determined that compounds other than CO2, O2, CO and N2 are not present in concentrations sufficient to affect the results. Sample was collected utilizing an integrated technique and analyzed using an Orsat gas analyzer. Several analyses were performed during each test run to ensure a stable reading. The Orsat was checked for leaks prior to each use. Chemicals were changed frequently and evaluated for reactivity prior to each use.

GE EnergyProject

## M22A0346B Rev.1 

# 4

# GE Energy

4.4 Determination of the Concentration of Gaseous Pollutants Using the Multi-Pollutant Sampling System 

## Concentrations of NOx 

## were determined using one sampling system. Sample was drawn from the source through a heated, extractive probe equipped with an in-stack filter. The probe was equipped with a fitting that allowed the probe to be flooded with calibration gas. A length of Teflon ® tubing connected the extractive probe to the sample conditioning system. The sample was routed through Teflon® tubing to a manifold. The manifold controlled the flow rate of gases sent to each of the affected analyzers. The manifold also controlled the flow rate of calibration gases sent to the extractive sample probe. The voltage output of each analyzer was continuously recordedvia an electronic data logger. The data logger generated a file consisting of oneminute average pollutant concentrations. This data was transferred to an Excel spreadsheet and then averaged over the appropriate time interval.
4.4.1 NOx 

## Determination by USEPA Method 7E 

## This method is applicable in the determination of NOx 

## concentrations in controlled and uncontrolled emissions from stationary sources only when specified within the regulations. The NO x 

## analyzer used a photomultiplier tube to measure the light emitted from the chemiluminescent decomposition of N02. As the analyzer does not "routinely measure emissions below 

# 20 ppm", a Manufacturer's Stability Test was not required. An interference test was performed on this analyzer prior to August 14, 

# 2006 in accordance with the preAugust 14, 

# 2006 version of Method 

# 20. As such, the interference test specified in Method 7E 

## was not required. The converter efficiency test required by Method 7E 

## was performed prior to the test. Prior to sampling, the linearity of the analyzer was established using EPA Protocol One high-range, mid-range and zero gases. The system response time was determined by measuring the time required for the system to respond to within 95% of the analyzer span to one of the up-scale gases and the zero gas. Prior to and following each sample run, the zero gas and one up-scale gas were introduced to the system to quantify system bias and drift. 4.5 Moisture Determination by USEPA Method 4 

## This method is applicable for determining the moisture content of stack gas. Sample was drawn from the source through a stainless steel probe equipped with an in-stack filter. A short length of Teflon® tubing connected the probe to an impinger train.

GE Energy Project M22A03468 Rev.1 

# 5

# GE Energy

The impinger train was followed in series by a pump and a dry test meter. Each of the first two impingers was filled with approximately 100 mls of water; the third impinger was left empty; and the fourth impinger was filled with approximately 200 grams of indicating silica gel. Each of the impingers was pre-weighed to the nearest 0.1 gram, and placed in an ice bath. Upon successful completion of the pre-test leak check, the probe was inserted into the stack/duct and the pump activated. Sample was collected at a constant rate of approximately 0.75 cubic feet per minute for the duration of the test. The duration of the test was such that a minimum of 21 dry standard cubic feet of sample was collected. At the conclusion of the sample run, a leak check of the sampling train was performed at a vacuum greater than that encountered during sampling. Following the leak check, any moisture on the exterior of the impingers was removed, and each impinger was reweighed to the nearest 0.1 gram.

5.0 QUALITY ASSURANCE PROCEDURES 

## GE Energy recognizes the previously described reference methods to be very technique oriented and attempts to minimize all factors which can increase error by implementing its Quality Assurance Program into every segment of its testing activities. Dry test meters are calibrated according to methods described in the 

## Quality Assurance Handbook for Air Pollution Measurement Systems, Volume III, Stationary Source Specific Methods, USEPA 600/R-94/038c, September 1994, Method 5. Calibration gases are EPA Protocol gases.

GE Energy Project M22A0346B Rev.1 

## 6

# GE Energy

6.0 TEST RESULTS SUMMARY

1 05/01/07

93 92 95 93 54.4 54.5 54.5 54.5 0.04 0.04 0.04 0.04 20.0 20.0 20.0 20.0 0.5 0.5 0.5 0.5 28.46 28.42 28.48 28.45 194581 194762 194855 194733 184169 184675 183874 184240 176898 177047 177021

7:50 9:00 8:50 10:00 0.3 0.3 0.3 20.3 20.3 20.3 31.2 35.8 33.2 39.54 45.41 42.10

GE Energy Project M22A0346B Rev.1 

# 7

# GE Energy

1 05/01/07

95 93 94 94 54.2 52.3 53.2 53.2 0.04 0.04 0.05 0.05 20.0 20.0 20.0 20.0 0.5 0.5 0.5 0.5 28.42 28.42 28.30 28.38 193671 187146 190177 190331 182839 177239 179649 179909 169677 170102 171619

Run Start Time: 

## 7:50 9:05

un End Time: 

## 8:50 10:05 OxConcentration 

## 57.5 65.8 60.5 OxEmission Rate 

## 69.90 80.18 74.36

GE Energy Project M22A0346B Rev.1 

## 8

# GE Energy

GE Energy Project M22A0346B Rev.1 

## 1 05/01/07

102 102 102 102 60.9 60.7 61.0 60.9 0.09 0.08 0.09 0.08 19.5 19.6 19.6 19.6 0.6 0.6 0.6 0.6 27.95 27.99 27.94 27.96 217628 217001 218241 217623 140651 140277 141005 140644 128857 128844 128790

11:43 12:57 12:43 13:57

0.6 0.5 0.6 19.5 19.6 19.6 96.3 93.4 94.0 88.90 86.21 86.76



## 9

# GE Energy

1 05/01/07

117 51.7 0.07 19.9 0.7 28.14 184834 168754 156830 ASEOUS CONCENTRATION AND EMISSION RATE DATA Run Start Time: 14:13 Run End Time: 15:13 NOx

### Concentration 105.3 NO Emission Rate 118.31 113 51.7 0.08 20.0 0.7 28.02 184755 169849 155975

5:46 6:46 98.9 110.51 

## 3 05/02/07

113 51.6 0.07 20.0 0.7 28.12 184532 169434 157102

7:00 8:00 97.8 110.07 114 51.7 0.08 20.0 0.7 28.09 184707 169346 156635

100.7 112.96

GE Energy Project M22A0346B Rev.1 

# 10

# GE Energy

1 05/02/07

106 48.1 0.07 20.0 0.5 28.08 172058 160165 148385 ASEOUS CONCENTRATION AND EMISSION RATE DATA un Start Time: 8:37 Run End Time: 9:37 NOx

### Concentration 104.2 NOx 

### Emission Rate 110.77 107 47.6 0.07 19.3 0.7 28.12 170048 158258 147133

10:42 11:42 109.4 115.31 

## 3 05/02/07

110 47.4 0.08 20.1 0.6 28.06 169343 156707 144590

11:57 12:57 114.3 118.40 108 47.7 0.07 19.8 0.6 28.09 170483 158377 146703

109.3 114.83

GE Energy Project M22A03468 Rev.1 

# 11

# GE Energy

05/02/07

103 50.6 0.06 20.0 0.5 28.21 180846 169342 158858 GASEOUS CONCENTRATION AND EMISSION RATE DATA Run Start Time: 13:11

un End Time: 14:11 Ox Concentration 105.3 

# o Emission Rate 119.84 101 49.9 0.07 19.3 0.7 28.17 178533 167735 156739

14:32 15:32 104.7 117.57 102 53.1 0.06 20.1 0.6 28.26 189663 177897 167478

5:45 6:45 100.5 120.58 102 51.2 0.06 19.8 0.6 28.21 183014 171658 161025

103.5 119.33

GE Energy Project M22A0346BRev.1 

# 12

# GE Energy

1 2 05/03/07 05/03/07

96 96 97 96 51.7 51.5 51.1 51.4 0.07 0.07 0.07 0.07 20.0 20.0 20.0 20.0 0.5 0.5 0.4 0.5 28.14 28.17 28.14 28.15 184879 183993 182729 183867 175431 174420 172847 174233 161383 162653

Run Start Time: 

## 8:13 9:33 Run End Time: 

## 9:13 10:33 NOx

### Concentration 

## 67.8 68.7 68.1



# o Emission Rate 

## 79.18 79.43 79.35

GE EnergyProjectM22A0346B Rev.1 

## 13

# GE Energy

1 05/03/07

89 90 92 90 54.2 54.5 54.5 54.4 0.06 0.06 0.06 0.06 20.0 20.0 20.0 20.0 0.5 0.5 0.5 0.5 28.18 28.20 28.24 28.20 193718 194934 194815 194489 186150 186794 186158 186368 175203 174805

Run Start Time: 12:10 13:26 Run End Time: 13:10 14:26 NOx 

### Concentration 52.3 53.8 52.9 NOx 

### Emission Rate 65.59 67.53 66.25

GE Energy Project M22A0346B Rev.1 

## 14

# GE Energy

1 2 3 05/08/07 05/08/07 05/08/07

97 98 97 98 56.8 58.0 58.3 57.7 0.08 0.10 0.07 0.08 19.0 19.0 19.0 19.0 0.5 0.5 0.5 0.5 28.00 27.79 28.04 27.94 202928 207393 208374 206231 190147 193727 194993 192956 175397 175024 180607 177009 GASEOUS CONCENTRATION AND EMISSION RATE DATA Run Start Time: 

## 10:52 12:02 13:12 Run End Time: 

## 11:52 13:02 14:12 NOx 

### Concentration 

## 33.8 32.4 30.8 32.3 NOx 

### Emission Rate 

## 42.47 40.63 39.85 40.98

GE EnergyProjectM22A0346BRev.1 

## 15

# GE Energy

0.08 0.08 101 102

0.5 102 57.5

19.0 0.08

47.5 27.94

59.43 190619 205386

174690 103



## 3

19.0 0.5 0.09 56.3

9:32

48.7 27.91

10:32

59.48 170494 186415 201264 05/08/07

9:19 8:19

47.0 59.49 0.6 0.5 19.0 19.0 58.0 58.1

27.97 27.93

192611 192830 176885 176690 207291 207604 05/08/07

un End Time: 8:08 Ox Concentration 46.8 Ox Emission Rate 59.31 GASEOUS CONCENTRATION AND EMISSION RATE DATA Run Start Time: 7:08

GE EnergyProjectM22A0346BRev.1 

# 16

# GE Energy

1 05/07/07

115 111 113 113 54.4 55.9 52.6 54.3 0.07 0.06 0.08 0.07 20.0 19.0 19.0 19.3 0.5 0.5 0.5 0.5 28.17 28.15 27.95 28.09 194503 199996 188072 194191 176584 182699 184116 181133 169084 168402

Run Start Time: 6:11 7:38 Run End Time: 7:11 8:38 NOx 

### Concentration 68.5 68.6 68.8 NOx 

### Emission Rate 83.93 83.10 83.04

GE Energy Project M22A0346B Rev.1 

# 17

# GE Energy

1 05/07/07



### 123 123 56.3 56.6 0.06 0.06 19.0 19.0 0.6 0.5 28.22 28.19 201346 202366 180054 181173 169542 170277 GASEOUS CONCENTRATION AND EMISSION RATE DATA 

## 3 05/08/07



### 120 56.1 0.08 19.0 0.5 27.94 200712 180583 165626 122 56.4 0.07 19.0 0.5 28.12 201475 180603 168482

Run Start Time: 14:22 Run End Time: 15:22 NO x 

### Concentration 100.9 NO x 

### Emission Rate 122.55 15:39 16:39 97.2 118.57 5:55 6:55 102.7 121.86 100.3 120.99

GE Energy Project M22A0346B Rev.1 

# 18

# GE Energy

Furnace Line No.



## 2



## 3 Emission Source

SV021 SV022 SV023 SV024 Total SV025 SV026 SV027 SV028 Total SV029 SV030 SV031 SV032 Total NOx Emission Rate/Source Ib/hr 42.1 74.36 86.76 112.96 316.18 114.83 119.33 79.35 66.25 379.76 40.98 59.43 83.04 120.99 304.44 Average NOx Emission Rate

3.63

3.75

2.92

*Total NOx Emission Rate (Ib/hr) 

### IAverage Heat Input (MMBtu/hr) for each Furnace Line

GE Energy Project M22A0346B Rev.1 

## 19

## APPENDIX



# 20

## M22A03468 Project Participants

Hibbing Taconite Representative Andrea Hayden GE Energy Project Manager Michael Anderson GE Energy Test Crew Travis Worsech, Randy Bergstrom



# 21

# ~. 

# - 

# - Mlnnesot2 Pollution Control Agency 

### MinnesotaPollution ControlAgency 520 LafayetteRd. N. SaintPaul, MN 55155-4194(651)-296-6300

Test Date(s):**~M.,.aY,::-:,-I-=2,=2"",O,,-,07,--:---,-** 

### _ Company Name: HibbingTaconite Company Furnace(s) No: LineNo. I

A. Fuel Input 

### & Operating Capacities: Itemize fuels and materials added to the combustion process during the test period. Attach ultimate/proximate analysis ofthe fuel, ifapplicable. LIST APPROPRIATE UNITS.

Run#& FueiType & 

### Origin Fuel Input Heatcl!Jltent I 

### S.team·....•.. •·•..· .• G..oss lIeatInput Stack Vent # (e.g, 

### Bituminous/Eastern) (MCF/hr) .(MMBtu/MCF) (103lbs./hour)<IMW/hOur I (MMBtu/llr) Run 1 SV021 Natural Gas 77 1.015 NA NA 78 Run 2 SV021 Natural Gas 

### 72 1.015 NA NA 73 Run 3 SV021 Natural Gas 87 1.015 NA NA 88 Avg. Natural Gas 79 1.015 NA NA 80 Run 1 SV022 Natural Gas 77 1.015 NA NA 78 Run 2 SV022 Natural Gas 71 1.015 NA NA 

### 72 Run 3 SV022 Natural Gas 99 1.015 NA NA 100 Avg. Natural Gas 82 1.015 NA NA 83 Run 1 SV023 Natural Gas 81 1.015 NA NA 82 Run 2 SV023 Natural Gas 85 1.015 NA NA 86 Run 3 SV023 Natural Gas 103 1.015 NA NA 104 Avg. Natural Gas 90 1.015 NA NA 91 Run 1 SV024 Natural Gas 101 1.015 NA NA 102 Run 2 SV024 Natural Gas 87 1.015 NA NA 89 Run 3 SV024 Natural Gas 91 1.015 NA NA 92 Avg. Natural Gas 93 1.015 NA NA 94



## B. OperatingDataforFurnace and AirPollution Control Equipment: 1. 

## Were the furnace(s) and control equipment operated consistent with normal procedures? YES 2, Date(s) and procedure(s) oflast maintenance/cleaning within 6 months: January 25, 2007-February 11,2007 3. Include a copy ofchart/datalog records during test for the combustion efficiency indices (carbon monoxide (CO), oxygen (02), carbon dioxide, (C02), combustibles, steam flow, air flow, etc.) Label as appropriate, 4. Soot blowing and ash pulling information: No soot blowing or ash pulling conducted, go to item 5 

# 22 Page 1 of3

## 5. Summarize control equipment operating data documented during testing. Values reported should reflect maximum, minimum, averages, or as approved in the test plan. (See test plan and approval letter)

Examples ofAPe 

### equipment and parameters generally monitored. Monitor as in the test plan and/or approval letter. • Scrubber (list type ofscrubber): M 

### (in. w.c.)and feedrate(gpm andpsig) 

## I • Baghouse, Cyclone, and Multi-clone: dP (in. w.c.) • Catalytic Incinerator :(OFinlet ,oFoutlet) 

### and Thermal Incinerator: (OFoneratin.) 

## I • ESP: Numberandidentity of orcratingfield(s) APCequipmentand parameter monitored 

### RunI' 

## 'Run2' Run 3

" ,

### A.v~rll~e 

### SV021 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.51 0.51 0.50 0.51 SV021 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.48 0.47 0.47 0.47 SV021 Demist Panel**~P** 

### Average (in. H2O) 

### 0.49 0.48 0.48 0.48 SV021 Venturi**~P** 

### Maximum (in. H2O) 

### 4.08 3.87 3.68 3.88 SV021 Venturi**~P** 

### Minimum (in. H2O) 

### 3.31 3.31 2.94 3.19 SV021 Venturi**~P** 

### Average (in. H2O) 3.56 3.53 3.40 3.50 SV022 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.42 0.44 0.42 0.43 SV022 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.40 0.39 0.39 0.39 SV022 Demist Panel**~P** 

### Average (in. H2O) 

### 0.41 0.41 0.41 0.41 SV022 Venturi**~P** 

### Maximum (in. H2O) 

### 5.20 5.22 5.17 5.20 SV022 Venturi**~P** 

### Minimum (in. H2O) 

### 4.90 4.86 4.92 4.89 SV022 Venturi**~P** 

### Average (in. H2O) 5.07 5.05 5.05 5.06 SV023 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.59 0.59 0.56 0.58 SV023 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.51 0.50 0.53 0.51 SV023 Demist Panel**~P** 

### Average (in. H2O) 

### 0.55 0.55 0.55 0.55 SV023 Venturi**~P** 

### Maximum (in. H2O) 

### 4.38 4.38 4.11 4.29 SV023 Venturi**~P** 

### Minimum (in. H2O) 

### 3.42 3.32 3.32 3.35 SV023 Venturi**~P** 

### Average (in. H2O) 3.81 3.80 3.73 3.78 SV024 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.33 0.33 0.34 0.33 SV024 Demist Panel**~P** 

### Minimum (in. H2O) 

# - 0.30 0.32 0.31 0.31 SV024 Demist Panel**~P** 

### Average (in. H2O) 

### 0.32 0.33 0.32 0.32 SV024 Venturi**~P** 

### Maximum (in. H2O) 

### 4.45 4.46 4.54 4.48 SV024 Venturi**~P** 

### Minimum (in. H2O) 

### 4.07 4.10 4.05 4.07 SV024 Venturi**~P** 

### Average (in. H2O) 4.22 4.32 4.33 4.29

Abbreviations: APe-airpollutioncontrol Btu-britishthermal units gpm.-gallons per minute in.w.c.-inches of watercolumn lbs.-pounds MW-megawatts psig-pressurepersquareinchgauge dP- pressuredrop



# 23 Page 2 of3

### Examples of

### APe equipment and parameters generally monitored. Monitor as in the test plan and/or approval letter

. • Scrubber (list type ofscrubber):**~p** 

### (in. w.c.) and feed rate (gpm and psig) • Baghouse, Cyclone, and Multi-clone:**~p** 

### (in. w.c.) • Catalytic Incinerator :(OPinlet ,oFoutlet) 

### and ThermalIncinerator: (OFonerntin_) 

### • ESP: Numberand identityofoperatingfield(s) APCequipmentand parameter monitored 

## Rull]

..·.·.' . 

### R.uri\2

.... 

## R.un3········ I 

### Average 

### SV021 Water Flow Rate Maximum (gpm) 

### 1061 1078 1057 1065 SV021 Water Flow Rate Minimum (gpm) 

### 1024 1037 1037 1033 SV021 Water Flow Rate Average (gpm) 

### 1047 1058 1047 1051 SV022 Water Flow Rate Maximum (gpm) 

### 1038 1036 1034 1034 SV022 Water Flow Rate Minimum (gpm) 

### 1012 1002 1013 1009 SV022 Water Flow Rate Average (gpm) 

### 1024 1026 1024 1025 SV023 Water Flow Rate Maximum (gpm) 

### 1103 1103 1078 1095 SV023 Water Flow Rate Minimum (gpm) 

### 1050 1046 1049 1048 SV023 Water Flow Rate Average (gpm) 

### 1079 1077 1062 1073 SV024 Water Flow Rate Maximum (gpm) 

### 663 672 669 668 SV024 WaterFlow Rate Minimum (gpm) 

### 649 661 658 656 SV024 WaterFlow Rate Average (gpm) 

### 655 667 662 661
Abbreviations: APe-air pollutioncontrol Btu.-britishthermalunits gpm.-gallons per minute in. w.c.-inches of watercolumn Ibs.-pounds MW-megawatts psig-pressureper square inch gauge M- pressuredrop

Run No. Fired Pellets Bentonite Usage Moisture Content Limestone Addition Rate (dltlhr) (#/dlt) (% H2O) 

### (%/dlt) Run I 

### SV021 370 17.68 9.58 0.29 Run 

### 2 SV021 373 17.68 9.51 0.29 Run 

### 3 SV021 371 17.68 9.51 0.29 Run I 

### SV022 371 17.68 9.58 0.29 Run 

### 2 SV022 372 17.68 9.51 0.29 Run 

### 3 SV022 372 17.68 9.51 0.29 Run I 

### SV023 371 17.68 9.32 0.28 Run 

### 2 SV023 371 17.68 9.51 0.29 Run 

### 3 SV023 365 17.68 9.51 0.30 Run I 

### SV024 372 17.68 9.51 0.30 Run 

### 2 SV024 365 17.72 9.81 0.30 Run 

### 3 SV024 351 17.72 9.81 0.30

NOTE: This formprovides only a summary of the operating conditions during theperformance test. Additionaland more detailed records are required to meet the requirements of Minn. R. 7017.2035. Thisform is to be submitted as part of the performance test report 

### aq-f6-ST04 

# Page 3 of3 

# 24 Form ST-04, Page 1 of 1

# l\U~~~s~t~POllutionc()fifrolA.gen~~i\: ..

# ·?i~>: ••••... < •..•.•..•....."

..' 

### 5tOLa

..

## ~yette.J.{~. 

# -N' SaihtPaul, MN

## 5515?~4194(65n:.29~-~300**'~."** 

# ': -:**!·Q~~~@!i~·~** 

# •.•••.**I>~!a.·.Su~~~ry** 

# ••.**~~r** ••.

# ·coni.·~lis·ti~.~.·.···.S~lI.~.~.e~ 

# •••::::
.**Mlnnesot~:·** '::**~olilJtlor1.**

Control .•• 

### Agenc:}1

TestDate(s): ""M""aYJ-Z"'--"""3,

.... Z""O"'-07'---

_ Company Name: Hibbing Taconite Company Furnace(s) No: Line No. Z



### A. Fuel Input & 

### Operating Capacities: Itemize fuels and materials added to the combustionprocess during the test period. Attach ultimate/proximate analysis ofthe fuel, ifapplicable. 

### LISTAPPROPRIATE UNITS.**~~ni#&**

# ··:····:·I:'·~e.~·]lt!~f:o~$~~;:~rn) Fuellriput Heatcontent .•.•••.Stealn.·i·········

# I.**Gr~ss** 

### '.}leatInput. StackVenf#

.(l\iCFlhr) 

### (MMBtu/MCF) (103 

### Ibs.lhour) ,. ····MW/hour··•.'. ···.·(MMBtu/hr)

. 

### Run 

### 1 SV025 Natural Gas 

### 95 1.015 NA NA 

### 96 Run 2 SV025 Natural Gas 

### 99 1.015 NA NA 

### 101 Run 3 SV025 Natural Gas 

### 101 1.015 NA NA 

### 103 Avg. Natural Gas 

### 98 1.015 NA NA 

### 100 Run 

### 1 SV026 Natural Gas 

### 103 1.015 NA NA 

### 104 Run 2 SV026 Natural Gas 

### 103 1.015 NA NA 

### 104 Run 3 SV026 Natural Gas 

### 103 1.015 NA NA 

### 104 Avg. Natural Gas 

### 103 1.015 NA NA 

### 104 Run 

### 1 SV027 Natural Gas 

### 102 1.015 NA NA 

### 104 Run 2 SV027 Natural Gas 

### 102 1.015 NA NA 

### 104 Run 3 SV027 Natural Gas 

### 105 1.015 NA NA 

### 106 Avg. Natural Gas 

### 103 1.015 NA NA 

### 105 Run 

### 1 SV028 Natural Gas 

### 102 1.015 NA NA 

### 104 Run 2 SV028 Natural Gas 

### 100 1.015 NA NA 

### 102 Run 3 SV028 Natural Gas 

### 102 1.015 NA NA 

### 104 Avg. Natural Gas 

### 101 1.015 NA NA 

### 103



## B. OperatingData for Furnace and AirPollution ControlEquipment: 1. Were the fumace(s) and control equipment operated consistent with normal procedures? YES 2. Date(s) andprocedure(s) oflastmaintenance/cleaning within 6 months: February 19 - March 16,2007 3. Include a copy ofchart/datalog records during test for the combustion efficiency indices (carbon monoxide (CO), oxygen (02), 

## carbon dioxide, (C02), 

## combustibles, steam flow, air flow, etc.) Label as appropriate. 4. Soot blowing and ash pulling information: No soot blowing or ash pulling conducted, go to item 5



## Page 1 of3

## 5. Summarize control equipment operating data documented during testing. Values reported should reflect maximum, minimum, averages, or as approved in the test plan. (See test plan and approval letter)

Examples ofAPe 

### equipment and parameters e:eneraHy monitored. Monitor as in the test plan and/or approval letter

. • Scrubber (list type of scrubber): AI' 

### (in. w.c.)and feedrate (gpmand psig) • Baghouse, Cyclone, andMulti-clone:**~p** 

### (in. w.c.) • CatalyticIncinerator :(OFinlet ,OFoutlet) 

### and ThermalIncinerator: (OF oneratin.) 

### • ESP: Numberandidentity ofoperatingfield(s)

'i'./:

.

### '.A]lCiequipmentand parameter monitored Runt' Rllu2 ·····llun3! ····.·:A:vera2e . 

### SV025 Demist Panel**~P** 

### Maximum (in. H2O) 

### 1.13 1.10 1.09 1.10 SV025 Demist Panel**~P** 

### Minimum (in. H2O) 

### 1.08 1.05 1.05 1.06 SV025 Demist Panel**~P** 

### Average (in. H2O) 

### 1.10 1.06 1.07 1.08 SV025 Venturi**~P** 

### Maximum (in. H2O) 

### 4.82 4.75 4.80 4.79 SV025 Venturi**~P** 

### Minimum (in. H2O) 

### 4.57 4.49 4.50 4.52 SV025 Venturi**~P** 

### Average (in. H2O) 4.68 4.62 4.59 4.63 SV026 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.91 0.89 0.89 0.90 SV026 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.84 0.83 0.85 0.84 SV026 Demist Panel**~P** 

### Average (in. H2O) 

### 0.87 0.86 0.87 0.87 SV026 Venturi**~P** 

### Maximum (in. H2O) 

### 5.63 5.48 4.61 5.24 SV026 Venturi**~P** 

### Minimum (in. H2O) 

### 4.74 4.58 3.53 4.28 SV026 Venturi**~P** 

### Average (in. H2O) 5.04 5.12 4.21 4.79 SV027 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.41 0.40 0.40 0.40 SV027 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.39 0.38 0.36 0.38 SV027 Demist Panel**~P** 

### Average (in. H2O) 

### 0.40 0.39 0.38 0.39 SV027 Venturi**~P** 

### Maximum (in. H2O) 

### 5.40 5.40 5.37 5.39 SV027 Venturi**~P** 

### Minimum (in. H2O) 

### 5.24 5.22 5.19 5.22 SV027 Venturi**~P** 

### Average (in. H2O) 5.32 5.32 5.29 5.31 SV028 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.59 0.58 0.57 0.58 SV028 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.49 0.54 0.52 0.52 SV028 Demist Panel**~P** 

### Average (in. H2O) 

### 0.54 0.56 0.55 0.55 SV028 Venturi**~P** 

### Maximum (in. H2O) 

### 4.38 4.32 4.24 4.31 SV028 Venturi**~P** 

### Minimum (in. H2O) 

### 3.66 3.67 3.75 3.69 SV028 Venturi**~P** 

### Average (in. H2O) 3.97 4.00 3.97 3.98

Abbreviations: APC-airpollution control Btu.-britishthermal units gpm.-gallons per minute in.w.c.-inches of watercolumn lbs.-pounds MW-megawatts psig-pressure persquareinchgauge AI'- 

### pressure drop



## Page 2of3

### Examples ofAPe equipment and parameters l!enerally monitored. Monitor as in the test plan and/or approval letter

. • Scrubber(list type ofscrubber): M 

### (in. w.c.) and feed rate (gpmand psig) • Baghouse, Cyclone, and Multi-clone: toP (in. w.c.) • Catalytic Incinerator :(OFinlet ,oFoutlet) 

### and ThermalIncinerator: (OFoneratin.) 

### • ESP: Numberandidentity ofoperatingfield(s) 

### I**"~"~';::,:** 

### ':

. ',,Al.'CeqiJipment**~Ildparll** 

### metermonito,red 

## ' ',!, Run 

## t "Run. 2 

## ':Rtiif3 

## ' Ii**'.Av~ra.2e**



### SV025 Water Flow Rate Maximum (gpm) 392 389 389 390 SV025 Water Flow Rate Minimum (gpm) 383 380 383 382 SV025 Water Flow Rate Average (gpm) 389 385 387 387 SV026 Water Flow Rate Maximum (gpm) 982 975 1030 996 SV026 Water Flow Rate Minimum (gpm) 960 964 997 974 SV026 Water Flow Rate Average (gpm) 970 969 1016 985 SV027 Water Flow Rate Maximum (gpm) 905 904 898 902 SV027 Water Flow Rate Minimum (gpm) 887 889 885 887 SV027 WaterFlow Rate Average (gpm) 893 898 891 894 SV028 Water Flow Rate Maximum (gpm) 1015 967 969 984 SV028 Water Flow Rate Minimum (gpm) 930 947 957 945 SV028 Water Flow Rate Average (gpm) 977 958 964 966

Abbreviations: APe-air pollutioncontrol Btu.-britishthermal units gpm-gallons per minute in.w.c.-inches of watercolumn Ibs.-pounds MW-megawatts psig-pressureper squareinchgauge M- 

### pressuredrop

Run No. Fired Pellets Bentonite Usage Moisture Content Limestone Addition Rate (dltlhr) (#/dlt) (% 

### H2O) 

### (%/dlt) Run 1 SV025 344 17.72 9.45 0.30 Run 2 SV025 362 17.72 9.53 0.30 Run 3 SV025 359 17.72 9.53 0.30 Run 1 SV026 363 17.72 9.53 0.30 Run 2 SV026 363 17.72 9.64 0.30 Run 3 SV026 358 17.63 9.40 0.30 Run 1 SV027 364 17.63 9.40 0.30 Run 2 SV027 366 17.63 9.47 0.30 Run 3 SV027 375 17.63 9.47 0.30 Run 1 SV028 360 17.63 9.59 0.30 Run 2 SV028 369 17.63 9.57 0.30 Run 3 SV028 375 17.63 9.57 0.30

NOTE: Thisformprovides only asummary of the operating conditions during theperformance test. Additionaland more detailed records are required tomeetthe requirements of Minn. R. 7017.2035. Thisform is to be submittedaspartof theperformancetest report. 

### aq-f6-ST04 

# Page 3 of3 Form ST-04,Page 1 of 1Mlnnesotf Pollution Control Agency 

# Operating

# DataSummaryForCombustionSources

Minnesota Pollution.ControlAgency

.520Lafayette Rd. N. SaintPaul, MN5S155-4194 (651)-296-6300 Form ST-04



## 6/9/06

TestDate(s): May 3 & 

### 7-8, 2007 Company Name: HibbingTaconite Company 

### Furnace(s) No:Line No.3



### A. Fuel Input & 

### Operating Capacities: Itemize fuels and materials added to the combustion process during the test period. Attach ultimate/proximate analysis ofthe fuel, ifapplicable. LIST APPROPRIATE UNITS

.**Run~&** 

### ...I·..FuelType &**Ori~in** 

### FllelInPllt Heat content: 

### . "<§tea

# rn Gross ijeatInput StackVent# .(e.z, 

### Bituminous/Eastern) (MCF/br)

.(MMBtuIMCF)': .U03lbs.lhClur) 

## MWlh'blir (MMBfu/hr) Run 1 SV029 Natural Gas 

## 103 1.015 NA NA 

## 104 Run 2 SV029 Natural Gas 

## 103 1.015 NA NA 

## 104 Run 3 SV029 Natural Gas 

## 102 1.015 NA NA 

## 104 Avg. Natural Gas 

## 103 1.015 NA NA 

## 104 Run 1 SV030 Natural Gas 

## 103 1.015 NA NA 

## 104 Run 2 SV030 Natural Gas 

## 103 1.015 NA NA 

## 104 Run 3 SV030 Natural Gas 

## 103 1.015 NA NA 

## 104 Avg. Natural Gas 

## 103 1.015 NA NA 

## 104 Run 1 SV031 Natural Gas 

## 101 1.015 NA NA 

## 102 Run 2 SV031 Natural Gas 

## 106 1.015 NA NA 

## 108 Run 3 SV031 Natural Gas 

## 106 1.015 NA NA 

## 108 Avg. Natural Gas 

## 104 1.015 NA NA 

## 106 Run 1 SV032 Natural Gas 

## 101 1.015 NA NA 

## 102 Run 2 SV032 Natural Gas 

## 101 1.015 NA NA 

## 103 Run 3 SV032 Natural Gas 

## 103 1.015 NA NA 

## 104 Avg. Natural Gas 

## 102 1.015 NA NA 

## 103



## B. OperatingData for Furnace and AirPollution Control Equipment: 1. Were the fumace(s) and control equipment operated consistentwith normal procedures? YES 2. Date(s) and procedure(s) of last maintenance/cleaning within 6 months: March 12, 2007-March 31, 2007 3. Include a copy ofchart/data log records during test for the combustion efficiency indices (carbon monoxide (CO), oxygen (02), carbon dioxide, (C02), combustibles, steam flow, air flow, etc.) Label as appropriate. 4. Soot blowing and ash pulling information: No sootblowing or ash pulling conducted, go to item 5



# Page 1 of3 

# 28

## 5. Summarize control equipment operating data documented during testing. Values reported should reflect maximum, minimum, averages, or as approved in the test plan. (See test plan and approval letter)

Examples ofAPe 

### equipment and parameters 2:enerally monitored. Monitor as in the testplan and/or approval letter. • Scrubber (list type ofscrubber): LlP (in. w.c.)and feed rate (gpmand psig) 

# I • Baghouse, Cyclone,and Multi-clone: LlP (in. w.c.) 

# I • CatalyticIncinerator :(OFinlet,°Foullet) 

### and Thermal Incinerator: (OF oDeratin.) 

# I • ESP: Numberandidentityofoperating field(s) 

## APC equipmentand parameter monitored' 

### Run! , 

### 'Rtiri2 . ' 

## 'RuD:3

.... 

## Average. ,< 

### SV029 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.37 0.37 0.36 0.37 SV029 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.33 0.33 0.34 0.33 SV029 Demist Panel**~P** 

### Average (in. H2O) 

### 0.35 0.35 0.35 0.35 SV029 Venturi**~P** 

### Maximum (in. H2O) 

### 5.30 5.25 5.08 5.21 SV029 Venturi**~P** 

### Minimum (in. H2O) 

### 4.66 4.86 4.74 4.75 SV029 Venturi**~P** 

### Average (in. H2O) 5.02 4.98 4.96 4.99 SV030 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.30 0.32 0.31 0.31 SV030 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.25 0.25 0.24 0.25 SV030 Demist Panel**~P** 

### Average (in. H2O) 

### 0.28 0.28 0.28 0.28 SV030 Venturi**~P** 

### Maximum (in. H2O) 

### 4.11 4.27 4.14 4.17 SV030 Venturi**~P** 

### Minimum (in. H2O) 

### 3.85 3.85 3.96 3.89 SV030 Venturi**~P** 

### Average (in. H2O) 3.98 4.04 4.04 4.02 SV031 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.33 0.35 0.34 0.34 SV031 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.26 0.31 0.30 0.29 SV031 Demist Panel**~P** 

### Average (in. H2O) 

### 0.30 0.33 0.33 0.32 SV031 Venturi**~P** 

### Maximum (in. H2O) 

### 3.42 2.90 2.92 3.08 SV031 Venturi**~P** 

### Minimum (in. H2O) 

### 2.73 2.62 2.59 2.65 SV031 Venturi**~P** 

### Average (in. H2O) 3.17 2.77 2.74 2.89 SV032 Demist Panel**~P** 

### Maximum (in. H2O) 

### 0.25 0.23 0.26 0.25 SV032 Demist Panel**~P** 

### Minimum (in. H2O) 

### 0.21 0.20 0.21 0.21 SV032 Demist Panel**~P** 

### Average (in. H2O) 

### 0.22 0.22 0.23 0.22 SV032 Venturi**~P** 

### Maximum (in. H2O) 

### 4.61 4.52 4.84 4.66 SV032 Venturi**~P** 

### Minimum (in. H2O) 

### 4.07 4.00 4.23 4.10 SV032 Venturi**~P** 

### Average (in. H2O) 4.27 4.31 4.42 4.33

Abbreviations: APC-airpollutioncontrol Btu.-britishthermal units gpm.-gallons per minute in.w.c.-inches of watercolumn lbs.-pounds MW-megawatts psig-pressure per square inch gauge M- 

### pressuredrop



# 29

Page 2 of3

### Examples of

### APe equipment and parameters generally monitored. Monitor as in the test plan and/or approval letter.

• Scrubber (list type ofscrubber): L'.P (in. w.c.) and feed rate (gpm and psig) 

## I • Baghouse, Cyclone, and Multi-clone: L'.P (in. w.c.) • Catalytic Incinerator :(OFinlet ,OFoutlet) 

### and ThermalIncinerator: (OFoDeratin.) 

## I • ESP: Number and identity of operatingfield(s) APC equipment and parameter monitored Runi ;: 

### RU:rL2>· Ji.Run j .....•. I 

### Average 

### SV029 WaterFlow Rate Maximum (gpm) 

### 724 705 703 711 SV029 Water Flow Rate Minimum (gpm) 

### 663 679 672 671 SV029 WaterFlow Rate Average (gpm) 

### 690 693 687 690 SV030 WaterFlow Rate Maximum (gpm) 

### 743 743 747 744 SV030 WaterFlow Rate Minimum (gpm) 

### 709 725 720 718 SV030 Water Flow Rate Average (gpm) 

### 724 733 737 731 SV031 WaterFlow Rate Maximum (gpm) 

### 676 688 693 686 SV031 WaterFlow Rate Minimum (gpm) 

### 649 663 648 653 SV031 WaterFlow Rate Average (gpm) 

### 661 675 666 667 SV032 WaterFlow Rate Maximum (gpm) 

### 520 525 520 522 SV032 WaterFlow Rate Minimum (gpm) 

### 509 503 501 504 SV032 WaterFlow Rate Average (gpm) 

### 515 516 509 513

Abbreviations: APe-airpollution control Btu.-britishthermal units gpm.-gallonsper minute in. w.c.-inchesof watercolumn Ibs.-pounds MW-megawatts psig-pressure per square inch gauge L'.P- 

### pressure drop

Run No. Fired Pellets Bentonite Usage Moisture Content Limestone Addition Rate (dlt/hr) 

### (#/dlt) (% H2O) 

### (%/dlt) Run I 

### SV029 373 17.65 9.51 0.28 Run 

### 2 SV029 378 17.65 9.76 0.27 Run 

### 3 SV029 370 17.65 9.76 0.27
Run I 

### SV030 373 17.65 9.59 0.27 Run 

### 2 SV030 360 17.65 9.77 0.27 Run 

### 3 SV030 375 17.65 9.77 0.27
Run I 

### SV031 377 17.63 9.64 0.35 Run 

### 2 SV031 372 17.63 9.81 0.35 Run 

### 3 SV031 361 17.63 9.81 0.35
Run 

### 1 SV032 376 17.79 9.47 0.30 Run 

### 2 SV032 377 17.79 9.47 0.30 Run 

### 3 SV032 375 17.65 9.59 0.27

NOTE: This form provides only a summary of the operating conditions during theperformance test. Additionaland more detailed records are required to meet the requirements of Minn. R. 7017.2035. This form is to be submitted as part of the performance test report. 

### aq-f6-ST04 

## Page 3 of3 

# 30 Form ST-04, Page 1 of 1

## 104.5" 

# n I
"'185" 2 TEST PORTS @ 

## 90' 

# o



# r TESTING PLATFORM ELEVATION



# '-



# -- 

# -- -- 

# -- -- 

# -- FROM SCRUBBER



# TEST PORT LOCATIONS HIBBING TACONITE COMPANY HIBBING, MINNESOTA



# 3:1

# GE Energy

S-Type Pitot Tube Manometer Assembly USEPAMethod 2

Leak-Free Connections

Gas Flow Flexible Tubing 0.64 em (0.25 

## in) Temperature Sensor 

# T

IIE--E



### 7.62 em (3 in)


# t 1.91 - 2.54 em 

## (.75 - 1.0 in)

# 1

:

# ~==

Manometer

Dwg-AD



# 32

# GE Energy

Multi-Component Gaseous Sampling Train
USEPA Methods 3A, 

## 6e, lE, or 10

3-Way Calibration Valve"""

Heated Probe In-Steck Filter
Calibration Gases 

## Heated Line



## Dwg-A Analyzer Options Available For System: 

## 1. NO

## x 2. O2 

### 3. CO2 

### 4. CO 

## 5. SO 2**n a** 

### Exhaust Data Recorder Flow Control



## GasAnalyzer



# 33 Moisture Removal System

Flow Control Valves

# GE Energy
Determination of Moisture Content in Stack Gases
USEPA Method 4

Heating Element 

# I-stack Wall 

# I

Probe (End packed with glass wool)

0.1. Water Empty Silica Gel

Air Tight Pump Vacuum By-Pass Valve

Rate Meter

Dry Gas Meter Surge Tank Ice Bath

Temperature Sensor 

## Dwg-T



# 34

### Company: Plant: Unit: Run: Hibbing Taconite Hibbing, MN 

## SV026 

## 1 Example Calculations Page 1 of 3



### Dry MolecularWeight

Md=

Wet MolecularWeight 

## 0.5 20.0 79.5

Ms

# = Md x (l-Bws) 

## + (18.0 x Bws)

Md 

# =

Ms= 28.88 Bws 

# = 0.06

MeterVolume at Standard Conditions
Vm(std) 

# = 17.647 x Y x Vm x (Pbar +AH/13.6) 

## Tm

y= AH 

# =
Vm(std) 

## = 1.005 2.00



## 24.553 24.005 521.0 Pbar

# = 29.90

Volume ofWater Vapor Condensed
Vwc(std) 

# =

33.6
Vwc(std) 

## =



# 3S

### Example Calculations Page 2 of 3


## Moisture Content

Bws 

# = Vwc(std) (Vwc(std)+Vm(std))

24.553

1.583 Vm(std) 

## =



# ----- ------ Vwc(std) 

# =
Bws=

Average Duct Velocity

Vs

# = 85.49 x Cp x 

## Sqrt**~p** 

### (avg) x (Ts (avg)/ (Ps x MS)Y 1 L


### Cp

# = 0.840 Tsavg

# = 563.1 

## Sqrt**~P** 

### (avg): 0.862 Ps = 29.86 Ms = 28.21



## Vs = 

## 50.60

Volumetric Flow Rate (Actual Basis)

Q= Vs x A x 60

Vs = 50.60 A= 59.583



## Q= 

## 180899

Volumetric Flow Rate (Standard Basis)

Qstd = 17.647 x Q x Ps Tsavg

Q= 180899 Ps = 29.86 Tsavg = 563.1



## Qstd = 

## 169293

## Example Calculations Page 3 of 3


## Volumetric Flow Rate (Standard Dry Basis) Qstd(dry) = Qstd x (1-Bws)



## Qstd = 

## Qstd{dry) 

## = 169293 Bws

# =
159041 0.061

Gas Concentration (02, C02, NOx or 502, ppm) Cgas =



# For: (C - CO) 

## x Cma (Cm - CO) 

# NOx

C=
Cma =



## Cgas

# =

GasEmission Rate (Ib/hr) 

# 104.3
218.1

105.3 CO 

# = -0.3 Cm

# = 216.4

Ib/hr 

# =

For: Cgas (dry) x MWgas x 

## 1.556E-07 X Qstd(dry)



# NOx

105.3 Cgas(dry)=



# ----- Mwgas = 

## 46.01

Ib/hr 

## = 119.84



# 37Customer: Location: Source: Hibbing Taconite Hibbing, MN SV021 Test Date: Job Number: Box Truck: Operator: 05/01/07 M22A0346 E11 MBA 

### NO. Calibration/Bias Calculations Project: M22A0346

Date: 05/01/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 -0.4 0.4 0.1 Pass Mid gas 218.1 218.4 0.3 0.1 Pass High gas 413.0 415.9 2.9 0.7 Pass

413 ISpan Value: Start End Time Time Run Cma Preeal Bias Posteal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 6:38 7:38 1 218.1 218.9 P 218.9. P P 1.3 P

. 1:3 . P P 

### ;,A;nt: 32.6 1.3 218.9 7:50 8:50 2 218.1 218.9 P 21.8,9 P P 1.3 P 1:3 P P 31.2 1.3 218.9 9:00 10:00 3 218.1 218.9 P 21.8:9 P P 1.3 P 

### .... 1.3 P P**:,.:~7.tJ** 35.8 1.3 218.9

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value of test Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 38

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run 

### # System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### 1.30 0.41 1.30 0.41 0.00 Upscale Gas 

### 218.87 0.11 218.90 0.12 0.01 2 Zero Gas 

### 1.30 0.41 1.30 0.41 0.00 Upscale Gas 

### 218.90 0.12 218.90 0.12 0.00 3 Zero Gas 

### 1.30 0.41 1.30 0.41 0.00 Upscale Gas 

### 218.90 0.12 218.90 0.12 0.00



# 39Date: Project: Customer: Location: Source: 5/1/2007 M22A0346 Hibbing Taconite Hibbing, MN SV021 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 1 Greater than 90%, TW/RBEnd- 6:30

Start- 6:00 TW/RB

Pressure, Barometric (Hg") : Pressure, Static (H20") : Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.61 0.50 29.65 0.840 104.52 Carbon Dioxide Content(\): Oxygen Content(\): Nitrogen Content(\): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 20.0 79.5 0.038 28.46 Rectangular Duct: Flue Area: inches by inches 59.583 sq. feet

Moisture Determination Initial Volume

. Final Volume •.............• Meter Temperature ....•••..• Meter Delta H •..••.•.... Meter Volume dscf.....••.••

Traverse Delta SORT Point: (M) (tip) A-l 0.68 0.8246 2 0.79 0.8888 3 0.89 0.9434 4 0.93 0.9644 5 0.93 0.9644 6 0.91 0.9539 7 0.90 0.9487 8 0.93 0.9644 9 0.95 0.9747 10 0.91 0.9539 11 0.90 0.9487 12 0.80 0.8944 544.137 567.937 45.0 2.0 24.872
Temp. (OF) 92 93 94 94 94 94 94 94 94 94 94 92 Meter Calibration ..•...... 1. 005 Imp. # Tare Final Net

1 750.2 765.2 15.0 2 731. 8 735.0 3.2 3 659.9 660.1 0.2 4 803.7 806.3 2.6 TOTAL 21.0

Traverse Delta SORT Temp. Point: (M) (tip) B-1 0.69 0.831 91 2 0.79 0.889 91 3 0.90 0.949 93 4 0.92 0.959 93 5 0.92 0.959 93 6 0.92 0.959 93 7 0.92 0.959 93 8 0.92 0.959 93 9 0.93 0.964 94 10 0.93 0.964 94 11 0.94 0.970 93 12 0.79 0.889 90

Average Delta (tiP): 0.8788
Average SORT Delta (tiP): .•..•.... 0.9365

Flue Gas Velocity,ft/sec: .....••. 54.428 Average Flue Temperature (Ts):............... 93.083333

Actual Vol. Flow Rate (acfm):.................. 194581
Dry Standard Flow Rate (dscfm) :........... 177118

Standard Flow Rate (scfm): .•.•••...•..•..••••... 184169



# 40Date: Project: Customer: Location: Source: 5/1/2007 M22A0346 Hibbing Taconite Hibbing, MN SV02l PITOT TRAVERSE DATA

Traverse Nwnber: Condition: Time: Data Taken By: 2 Greater than 90%, TW/RBEnd- 8:20

Start- 7:50 TW/RB

Pressure, Barometric (Hgll) : Pressure. Static(H20"): Pressure. Stack(Hg"): pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.61 0.50 29.65 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Plue Gas (Bws): Molecular Wt. of Gas. Wet: 0.5 20.0 79.5 0.042 28.422

Moisture**Dete~ination** Initial Volume •.......••.•• 568.211 Pinal Volume ..••..••...•... 591.392 Meter Temperature ......•••• 47.0 Meter Delta H 

## ........... 2.0 Meter Volume dscf......•.•. 24.130

Traverse Delta SQRT Temp. Point:**(~P)** (M) (op) A-l 0.69 0.8307 91 2 0.81 0.9000 91 3 0.90 0.9487 92 4 0.92 0.9592 92 5 0.92 0.9592 92 6 0.92 0.9592 92 7 0.92 0.9592 93 8 0.90 0.9487 93 9 0.91 0.9539 93 10 0.91 

### o. 9539 93 11 0.91 0.9539 93 12 0.79 0.8888 93 Rectangular Duct: Plue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration ...••••.. 1. 005

Imp. # Tare Final Net

1 765.2 781.1 15.9 2 735.0 739.2 4.2 3 660.1 661.0 0.9 4 806.3 807.8 1.5 TOTAL 22.5

Traverse Delta SQRT Temp. Point:**(~P)** (M) B-1 0.70 0.837 92 2 0.78 0.883 92 3 0.89 0.943 92 4 0.89 0.943 92 5 0.89 0.943 92 6 0.93 0.964 92 7 0.93 0.964 92 8 0.93 0.964 92 9 0.93 0.964 92 10 0.93 0.964 92 11 0.93 0.964 92 12 0.90 0.949 90

Average Delta**(~P):** .....•.•.•.... 0.8804
Average SQRT Delta**(~P)** : ..•...
. . . 0.9375

Flue Gas Velocity.ft/sec: .......• 54.479 Average Flue Temperature (Ts):............... 92.083333

Actual Vol. Flow Rate (acfm):.................. 194762
Dry Standard Flow Rate (dscfm) :........... 176898

Standard Flow Rate (scfm): ••••.•....•.•......... 184675



# 4:1Date: Project: Customer: Location: Source: 5/1/2007 M22A0346 Hibbing Taconite Hibbing, MN SV02l PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: Greater than 90%, TW/RB Start- 8:30 End- 9:00 TW/RB

Pressure, Barometric(HglI): Pressure, Static(H20n): Pressure, Stack(Hgn): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.61 0.50 29.65 0.840 104.52 Carbon Dioxide Content(\): Oxygen Content(\): Nitrogen Content(\): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 20.0 79.5 0.037 28.476 Rectangular Duct: Flue Area: 0.00 inches by 0.00 inches 59.583 sq. feet

Moisture Determination Initial Volume ..•......••.• 591.577 Final Volume ....••.......•• 615.399 Meter Temperature .......... 49.0 Meter Delta H 

### ........... 2.0 Meter Volume dscf......•..• 24.700

Traverse Delta SQRT Temp. Point: (tiP) (tip) (OF) A-I 0.69 0.8307 95 2 0.79 0.8888 95 3 0.90 0.9487 95 4 0.93 0.9644 95 5 0.93 0.9644 95 6 0.93 0.9644 95 7 0.90 0.9487 95 8 0.90 0.9487 95 9 0.96 0.9798 95 10 0.92 0.9592 95 11 0.90 0.9487 95 12 0.79 0.8888 93

Average Delta (tiP): 0.8788
Average SQRT Delta (tip) : ......•.• 0.9366

Flue Gas Velocity,ft/sec: ••...... 54.505 Meter Calibration .••.....• 1.005 Imp. # Tare Final Net

1 781.1 796.2 15.1 2 739.2 742.2 3.0 3 661. 0 661.0 0.0 4 807.8 809.9 2.1 TOTAL 20.2

Traverse Delta SQRT Temp. Point: (tip) (tip) B-1 0.70 0.837 95 2 0.80 0.894 95 3 0.85 0.922 95 4 0.91 0.954 95 5 0.92 0.959 95 6 0.93 0.964 95 7 0.93 0.964 95 8 0.93 0.964 95 9 0.91 0.954 95 10 0.91 0.954 95 11 0.91 0.954 93 12 0.85 0.922 93

Average Flue Temperature (Ts):............... 94.75

Actual Vol. Flow Rate (acfm):.................. 194855
Dry Standard Flow Rate (dscfm) :........... 177047

Standard Flow Rate (scfm): ••.•....••.••.•...••.. 183874



# 42Customer: Location: Source: Hibbing Taconite Hibbing, MN SV022 Test Date: Job Number: Box Truck: Operator: 05/01/07 M22A0346 E11 MBA 

### NO. Calibration/Bias Calculations Project: M22A0346

Date: 05/01/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 -0.4 0.4 0.1 Pass Mid gas 218.1 218.4 0.3 0.1 Pass High gas 413.0 415.9 2.9 0.7 Pass
Ispan Value: Start End Time Time Run Cma Precal Bias Posteal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 6:31 7:31 1 218.1 215.9 P 214:9 P P ,"0.4,'" P -0.2 P P 57.3..•, 58.2 -0.3 215.4 7:50 8;50 2 218.1 214.9 P 216.1 P P -0.2 P ····0:1. P P >,5!l;1' 57.5 -0.2 215.5 9:05 10:05 3 218.1 216.1 P 216.1 P P -0.1 P**~0.3** P P :'65:1 '. 65.8 -0.2 216.1

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value of test Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 43

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run 

### # System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### -0.40 0.00 -0.20 0.05 0.05 Upscale Gas 

### 215.90 -0.61 214.90 -0.85 -0.24 2 Zero Gas 

### -0.20 0.05 -0.10 0.07 0.02 Upscale Gas 

### 214.90 -0.85 216.10 -0.56 0.29 3 Zero Gas 

### -0.10 0.07 -0.33 0.02 -0.06 Upscale Gas 

### 216.10 -0.56 216.14 -0.55 0.01



# 44PITOT TRAVERSE DATA

Date: 5/1/2007 Traverse Nwnber: 1 Project: M22A0346 Condition: Greater than 90%, TW/RB Customer: Hibbing Taconite Time: Start- 7:20 End- 7:32 Location: Hibbing, MN Data Taken By: TW/RB Source: SV022

Pressure. Barometric (Hgn) : Pressure. Static (H20 n) : Pressure. Stack{Hgn): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.61 0.50 29.65 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content{%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas. Wet: 0.5 20.0 79.5 0.042 28.42 Rectangular Duct: Flue Area:

Moisture Determination Initial Volume •.•••.•...... Final Volume ..........•••.. Meter Temperature .•...•.... Meter Delta H .....•..... Meter Volume dscf.•.....•..

Traverse Delta SQRT Point: (Ap) (Ap) A-l 0.82 0.9055 2 0.89 0.9434 3 0.95 0.9747 4 0.95 0.9747 5 0.91 0.9539 6 0.87 0.9327 7 0.95 0.9747 8 0.96 0.9798 9 0.95 0.9747 10 0.93 0.9644 11 0.94 0.9695 12 0.64 0.8000 inches by 59.583

614.439 637.326 47.0 2.0 23.824
Temp. (oF) 94 96 96 96 96 96 96 96 96 96 93 91 inches sq. feet

Meter Calibration•..•..... 1. 005 Imp. # Tare Final Net

1 749.3 770.3 21.0 2 754.7 755.6 0.9 636.6 636.8 0.2 4 693.5 693.8 0.3 TOTAL 22.4

Traverse Delta SQRT Temp. Point: (Ap) (AP) B-1 0.82 0.906 93 2 0.90 0.949 93 3 0.93 0.964 93 4 0.91 0.954 94 5 0.93 0.964 95 6 0.88 0.938 95 7 0.86 0.927 96 8 0.85 0.922 96 9 0.85 0.922 96 10 0.78 0.883 96 11 0.76 0.872 92 12 0.60 0.775 87

Average Delta {Ap): 0.8679
Average SQRT Delta (Ap): ...•••.•• 0.9302

Flue Gas Velocity.ft/sec: ..•.••.• 54.173 Average Flue Temperature (Ts):............... 94.5

Actual Vol. Flow Rate (acfm):.................. 193671
Dry Standard Flow Rate (dscfm) :... ...•.•.. 175078

Standard Flow Rate (scfm): ..••.•.....•.......•.• 182839



# 45Date: Project: Customer: Location: Source: 5/1/2007 M22A0346 Hibbing Taconite Hibbing, MN SV022 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 2 Greater than 90%, TW/RBEnd- 8:25

Start- 8:15 TW/RB

Pressure, Barometric (HglI) : Pressure. Static(H20"): Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.61 0.50 29.65 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas. Wet, 0.5 20.0 79.5 0.043 28.416

Moisture Determination Initial Volume •..•....••.•. 637.447 Final Volume ....•••.•.••... 660.214 Meter Temperature ...•.••.•. 47.0 Meter Delta H 

## ........... 2.0 Meter Volume dscf........•• 23.699

Traverse Delta SORT Temp. Point:**(~p) (~P)**  (oF) A-I 0.78 0.8832 92 2 0.76 0.8718 92 3 0.79 0.8888 92 4 0.76 0.8718 93 5 0.83 0.9110 93 6 0.87 0.9327 92 7 0.95 0.9747 92 8 0.97 0.9849 92 9 0.96 0.9798 92 10 0.95 0.9747 92 11 0.94 0.9695 89 12 0.45 0.6708 86 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration••.•..... 1.005 Imp. # Tare Final Net

1 770.3 791.3 21.0 2 755.6 756.5 0.9 3 636.8 637.0 0.2 4 693.8 694.1 0.3 TOTAL 22 .4

Traverse Delta SORT Temp. Point:**(~P) (~p)**  B-1 0.76 0.872 95 2 0.87 0.933 95 3 1. 00 1.000 95 4 0.92 0.959 95 5 0.88 0.938 96 6 0.86 0.927 95 7 0.86 0.927 95 8 0.80 0.894 95 9 0.82 0.906 95 10 0.79 0.889 95 11 0.73 0.854 91 12 0.35 0.592 87

Average Delta**(~P):** ..••.•.....•.• 0.8188
Average SORT Delta**(~PJ:** ....•.•.• 0.9002

Flue Gas Velocity.ft/sec: ......•. 52.348 Average Flue Temperature (Ts):............... 92.75

Actual Vol. Flow Rate (acfm):.................. 187146
Dry Standard Flow Rate (dscfm) :........... 169677

Standard Flow Rate (scfm): ••..•.•.•••.....••••.. 177239



# 46PITOT TRAVERSE DATA

3 Greater than 90%, TW/RB Date: Project: Customer: Location: Source: 5/1/2007 M22A0346 Hibbing Taconite Hibbing, MN SV022 Traverse Number: Condition: Time: Data Taken By: Start- 9:23 TW/RB End- 9:33

Pressure, Static (H20U) : Pressure, Stack(HgU): Pitot Tube Coefficient (Cp) : Pressure, Barometric (HglI) :

79.5 20.0

28.302 0.5

0.053 Oxygen Content(%) : Carbon Dioxide Content(%):
Nitrogen Content(%): Water Vapor in Plue Gas (Bws): Molecular Wt. of Gas, Wet: 

### o. 00 inches sq. feet 29.61 0.50 29.65 0.840 104.52

inches by 59.583 0.00 Rectangular Duct: Duct Diameter (in):

Plue Area:

Moisture Determination Initial Volume .••.•.•.•..•. 660.289 Final Volume •.•.••......... 683.568 Meter Temperature .......... 46.0 Meter Delta H .0 ......... 2.0 Meter Volume dscf

.......... 24.280

Traverse Delta SQRT Temp. Point: (Ap) (Ap) (oF) A-l 0.73 0.8544 94 2 0.83 0.9110 94 3 0.84 0.9165 94 4 0.92 0.9592 94 5 0.87 0.9327 94 6 0.85 0.9220 94 7 0.90 0.9487 94 8 0.94 0.9695 94 9 0.91 0.9539 94 10 0.90 0.9487 94 11 0.92 0.9592 93 12 0.61 0.7810 91 Meter Calibration .......•• 1.005 Imp. # Tare Pinal Net

1 741. 7 722.5 -19.2 2 761.1 784.4 23.3 3 620.3 644.1 23.8 4 714.8 715.8 1.0 TOTAL 28.9

Traverse Delta SQRT Temp. Point: (Ap) (AP) B-1 0.70 0.837 95 2 0.85 0.922 95 3 0.85 0.922 95 4 0.87 0.933 95 5 0.90 0.949 95 6 0.89 0.943 95 7 0.85 0.922 95 B 0.86 0.927 95 9 0.81 0.900 95 10 0.81 0.900 95 11 0.77 0.877 95 12 0.63 0.794 91

Average Delta (Ap): •••••.•••••••• 0.8338 Average Plue Temperature (Ts):............... 94.166667
Average SQRT Delta (Ap): ••••••••• 0.9118 Actual Vol. Plow Rate (acfm):.................. 190177

Plue Gas Ve1oc1ty,ft/sec: .•••.•.• 53.196 Dry Standard Plow Rate (dscfm) :........... 170102

Standard Flow Rate (scfm): 179649



# 47Customer: Location: Source: Hibbing Taconite Hibbing, MN SV023 Test Date: Job Number: Box Truck: Operator: 05/01/07 M22A0346 E11 MBA 

### NO. Calibration/Bias Calculations Project: M22A0346

Date: 05/01/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 "0.4 0.4 0.1 Pass Mid gas 218.1 '. 218;4 0.3 0.1 Pass High gas 413.0 415.9 2.9 0.7 Pass
Ispan Value: 4131 Start End Time Time Run Cma Precal Bias Postcal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 10:25 11:25 1 .218.1 216.1 P 216.8 P P "0.3 ...... P -0:3. .: P P 'i 9106 92.4 -0.3 216.5 11:43 12:43 2 218.1 216.8 P 216.0 P P -0.3 P I'OT·.:· P P 

### 9$,7:> 96.3 0.2 216.4 12:57 13:57 3 218.1 216.0 P 215.0 P P 0.7 P 

### .0,4 P P 92;6 93.4 0.6 215.5

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run 

### # System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### -0.33 0.02 -0.31 0.02 0.00 Upscale Gas 

### 216.14 -0.55 216.78 -0.39 0.15 2 Zero Gas 

### -0.31 0.02 0.70 0.27 0.24 Upscale Gas 

### 216.78 -0.39 216.05 -0.57 -0.18 3 Zero Gas 

### 0.70 0.27 0.40 0.19 -0.07 Upscale Gas 

### 216.05 -0.57 214.96 -0.83 -0.26



# 49Date: Project: Customer: Location: Source: 5/1/2007 M22A0346 Hibbing Taconite Hibbing, MN SV023 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 1 >90%

Start- 10:51 MBA End- 11: 02

Pressure, Barometric (Hg") : Pressure, Static(H20"): Pressure, Stack(Hg"): pitot Tube Coefficient (Cp) : Duct Diameter (in): 20.61 -0.50 20.57 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%) : Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.6 19.5 79.9 0.085 27.95 Rectangular Duct: Flue Area:

Moisture Determination Initial Volume .••.•.......• Final Volume .......••.••..• Meter Temperature .•••...... Meter Delta H .•.......•. Meter Volume dscf .•.•..•...

Traverse Delta SQRT Point: (lip) (lip) A-l 0.73 0.8544 2 0.75 0.8660 3 0.78 0.8832 4 0.80 0.8944 5 0.80 0.8944 6 0.81 0.9000 7 0.75 0.8660 8 0.72 0.8485 9 0.74 0.8602 10 0.72 0.8485 11 0.73 0.8544 12 0.67 0.8185 inches by 59.583

683.925 707.053 48.0 2.0 16.760
Temp. (OF) 102 102 102 102 102 102 102 102 102 102 102 102 inches sq. feet

Meter Calibration•..•...•• 1.005

Imp. # Tare Final Net

1 755.5 876.7 121. 2 2 775.0 683.9 -91.1 3 519.4 519.6 0.2 4 759.4 762.2 2.8 TOTAL 33.1

Traverse Delta SQRT Temp. Point: (lip) (lip) B-1 0.66 0.812 101 2 0.73 0.854 101 3 0.72 0.849 102 4 0.70 0.837 103 5 0.66 0.812 103 6 0.74 0.860 103 7 0.77 0.877 103 8 0.74 0.860 103 9 0.77 0.877 103 10 0.77 0.877 103 11 0.77 0.877 101 12 0.64 0.800 100

Average Delta (lip) : 0.7363
Average SQRT Delta (lip) : ...•.•.•. 0.8576

Flue Gas Veloc1ty,ft/sec: ....•••. 60.875 Average Flue Temperature (Ts):............... 102.08333

Actual Vol. Flow Rate (acfm):.................. 217628
Dry Standard Flow Rate (dscfm) :........... 128670

Standard Flow Rate IscfmJ: •••...•••....•..•..... 140651



# 50Date: Project: Customer: Location: Source: 5/1/2007 M22A0346 Hibbing Taconite Hibbing, MN SV023 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 2 ,90%

Start- 12:07 MBA End- 12:19

Pressure, Barometric (HglI) : Pressure. Static(H20"): Pressure. Stack(Hg"): pitot Tube Coefficient(Cp) : Duct Diameter (in): 20.61 -0.50 20.57 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in P1ue Gas (Bws): Molecular Wt. of Gas. Wet: 0.6 19.6 79.8 0.081 27.994

Moisture Determination Initial Volume •.....•.••.•. 707.348 Final Volume ....••.••...... 730.748 Meter Temperature .......... 54.0 Meter Delta H 

## ........... 2.0 Meter Volume dscf•..•...... 16.759

Traverse Delta SQRT Temp. Point: (Ap) (Ap) (op) A-l 0.76 0.8718 102 2 0.78 0.8832 102 3 0.84 0.9165 102 4 0.84 0.9165 102 5 0.80 0.8944 102 6 0.77 0.8775 102 7 0.79 0.8888 103 8 0.78 0.8832 103 9 0.72 0.8485 103 10 0.73 0.8544 103 11 0.70 0.8367 103 12 0.68 0.8246 100 Rectangular Duct: P1ue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration.....•.•• 1.005

Imp. # Tare Pinal Net

1 876.7 905.9 29.2 2 683.9 684.1 0.2 3 519.6 520.0 0.4 4 762.2 763.9 1.7 TOTAL 31.5

Traverse Delta SQRT Temp. Point: (Ap) (Ap) B-1 0.62 0.787 102 2 0.65 0.806 102 3 0.67 0.819 102 4 0.69 0.831 102 5 0.72 0.849 102 6 0.72 0.849 102 7 0.75 0.866 102 8 0 ..79 0.889 102 9 0.77 0.877 102 10 0.75 0.866 102 11 0.74 0.860 102 12 0.56 0.748 98

Average Delta (Ap): ••....•.•..... 0.7342 Average Plue Temperature (Ts) : •.....•••..••.. 101.95833
Average SQRT Delta (Ap): ...••••.. 0.8560 Actual Vol. Plow Rate (acfm):.................. 217001

Plue Gas Veloc1ty.ft/sec: •.•...•. 60.699 Dry Standard Flow Rate (dscfm) : .••...••.•. 128857

Standard Flow Rate {scfm): ••..••..•..••......•.. 140277



# 51Date: Project: Customer: Location: Source: 5/1/2007 M22A0346 Hibbing Taconite Hibbing, MN SV023 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: >90% Start- 13:07 MBA End- 13:19

Pressure, Barometric (Hg") ; Pressure. Static(H20"): Pressure. Stack(Hg"): Pitot Tube CoefficientCCp): Duct Diameter (in): 20.61 -0.50 20.57 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas. Wet: 0.6 19.6 79.8 0.086 27.942 Rectangular Duct: Flue Area: 0.00 inches by 0.00 inches 59.583 sq. feet

Moisture Determination Initial Volume ...•.......•• 731.145 Final Volume •.••.......•.•. 754.486 Meter Temperature •.•.•....• 55.0 Meter Delta H 

### ........... 2.0 Meter Volume dscf....•.•... 16.685

Traverse Delta SQRT Temp. Point: (Ap) (AP) (oF) A-1 0.77 0.8775 102 2 0.80 0.8944 102 3 0.86 0.9274 102 4 0.81 0.9000 102 5 0.81 0.9000 102 6 0.80 0.8944 102 7 0.79 0.8888 103 8 0.74 0.8602 103 9 0.70 0.8367 104 10 0.72 0.8485 103 11 0.73 0.8544 103 12 0.70 0.8367 100

Average Delta (Ap): 0.7404
Average SQRT Delta (Ap): ...•.•... 0.8598

Flue Gas Ve1ocity.ft/sec: •....•.• 61.046 Meter Calibration ...•..... 1.005 Imp. # Tare Final Net 905.9 935.1 29.2 2 684.1 684.9 0.8 3 520.0 520.3 0.3 4 763.9 767.0 3.1 TOTAL 33.4

Traverse Delta SQRT Temp. Point: (Ap) (Ap) B-1 0.61 0.781 101 2 0.67 0.819 102 3 0.67 0.819 103 4 0.70 0.837 103 5 0.69 0.831 103 6 0.70 0.837 103 7 0.74 0.860 104 8 0.78 0.883 104 9 0.77 0.877 103 10 0.76 0.872 103 11 0.78 0.883 100 12 0.67 0.819 97

Average Flue Temperature (Ts):............... 102.25

Actual Vol. Flow Rate (acfm):.................. 218241
Dry Standard Flow Rate (dscfm) :....... .••• 128844

Standard Flow Rate (scfm): •.•.•••....••.•..•.•.. 141005



# 52Customer: Location: Source: Hibbing Taconite Hibbing, MN SV024 Test Date: Job Number: Box Truck: Operator: 5/1/2007

- 5/2/2007 M22A0346 E11 MBA 

### NO. Calibration/Bias Calculations Project: M22A0346

Date: 5/1/2007

- 5/2/2007
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 0.6 0.6 0.1 Pass Mid gas 218.1 217.0 1.1 0.3 Pass High gas 413.0 417.4 4.4 1.1 Pass
Ispan Value: Start End Time Time Run Cma Precal Bias Postcal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 14:13 15:13 1 218.1 215.0 P 214.0 P P '. 0:4 P I···· -0.3.: P P 103.T. 105.3 0.1 214.5 5:46 6:46 2 218.1 213.9 P 212.9· P P -0.3 P**-O:~** : P P 96$ 98.9 -0.3 213.4 7:00 8:00 3 218.1 212.9 P 217.6 P P -0.3 P I. -0.3 P P 96:4 97.8 -0.3 215.3

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value of test Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# S3

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run 

### # System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### 0.40 -0.05 -0.30 -0.22 -0.17 Upscale Gas 

### 214.96 -0.49 213.97 -0.73 -0.24 2 Zero Gas 

### -0.30 -0.22 -0.30 -0.22 0.00 Upscale Gas 

### 213.89 -0.75 212.90 -0.99 -0.24 3 Zero Gas 

### -0.30 -0.22 -0.30 -0.22 0.00 Upscale Gas 

### 212.90 -0.99 217.60 0.15 1.14



# 54PITOT TRAVERSE DATA

Date: 5/1/2007 Traverse Number: 1 Project: M22A0346 Condition: >90% Customer: Hibbing Taconite Time: Start- 14:30 End- 14: 40 Location: Hibbing, MN Data Taken By: TW/RB Source: SV024

Pressure, Barornetric(Hg"): Pressure, Static (H20") : Pressure, Stack{Hg"): Pitot Tube Coefficient (cp) : Duct Diameter (in): 29.86 -0.60 29.82 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.7 19.9 79.4 0.071 28.14 Rectangular Duct: Flue Area: inches by inches 59.583 sq. feet

Moisture Determination Initial Volume ..•..••.....• Final Volume

. Meter Temperature ••..•..•.. Meter Delta H

. Meter Volume dscf .••.••..•.

Traverse Delta SORT Point: (M) (.1.p) A-l 0.56 0.7483 2 0.70 0.8367 3 0.81 0.9000 4 0.84 0.9165 5 0.90 0.9487 6 0.91 0.9539 7 0.93 0.9644 8 0.87 0.9327 9 0.79 0.8888 10 0.76 0.8718 11 0.68 0.8246 12 0.54 0.7348 754.889 778.456 55.0 0.2 24.246
Temp. (OF) 117 117 117 117 117 117 117 117 117 117 117 115 Meter Calibration .......•• 1. 005 Imp. # Tare Final Net

1 935.1 678.0 -257.1 2 684.9 915.7 230.8 3 520.3 582.8 62.5 4 767.0 769.9 2.9 TOTAL 39.1

Traverse Delta SORT Temp. Point: (.1.P) (.1.P) B-1 0.61 0.781 117 2 0.65 0.806 117 3 0.71 0.843 116 4 0.79 0.889 116 5 0.81 0.900 116 6 0.82 0.906 117 7 0.87 0.933 117 8 0.82 0.906 117 9 0.82 0.906 117 10 0.73 0.854 117 11 0.71 0.843 117 12 0.58 0.762 113

Average Delta (.1.PI: 0.7588
Average SORT Delta (.1.PI : 0.8687

Flue Gas Ve1ocity,ft/sec: ••.•.... 51.702 Average Flue Temperature {Ts):............... 116.625

Actual Vol. Flow Rate (acfm):.................. 184834
Dry Standard Flow Rate (dscfm):.

... ....••• 156830

Standard Flow Rate (scfmj: •••.........•••••.•... 168754



# S5Date: Project: Customer: Location: Source: 5/2/2007 M22A0346 Hibbing Taconite Hibbing, MN SV024 PITOT**T~VERSE** DATA

Traverse Number: Condition: Time: Data Taken By: 2 >90%

Start- 6:11 TW/RB End- 6:20

Pressure, Barometric (HglI) : Pressure. StaticIH20"): Pressure. Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.86 -0.60 29.82 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content 1%) : Nitrogen Content(%): Water Vapor in Flue Gas IBws): Molecular Wt. of Gas. Wet: 0.7 20.0 79.3 0.082 28.021

Moisture Determination Initial Volume .•...••.•.. " 778.669 Final Volume ..•........•••. 801.477 Meter Temperature ..•....... 50.0 Meter Delta H

•••••• 0 •••• 2.0 Meter Volume dscf

.......... 23.800

Traverse Delta SORT Temp. Point: (M) lAp) (oF) A-1 0.55 0.7416 114 2 0.70 0.8367 114 3 0.75 0.8660 114 4 0.79 0.8888 114 5 0.85 0.9220 114 6 0.92 0.9592 114 7 0.85 0.9220 114 8 0.84 0.9165 114 9 0.79 0.8888 114 10 0.73 0.8544 114 11 0.66 0.8124 113 12 0.58 0.7616 110 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration .•....•.. 1.005 Imp. # Tare Final Net

1 721.1 764.4 43.3 2 695.8 695.8 0.0 3 621. 0 621. 5 0.5 4 715.8 716.9 1.1 TOTAL 44.9

Traverse Delta SORT Temp. Point: (Ap) 1M) B-1 0.57 0.755 113 2 0.69 0.831 113 3 0.72 0.849 113 4 0.86 0.927 112 5 0.85 0.922 113 6 0.91 0.954 112 7 0.88 0.938 110. 8 0.86 0.927 111 9 0.80 0.894 112 10 0.78 0.883 113 11 0.71 0.843 111 12 0.60 0.775 108

Average Delta (Ap): •.•.•....•••.• 0.7600
Average SORT Delta (APJ: .....••.. 0.8695

Flue Gas Ve1ocity.ft/sec: ......•. 51.680 Average Flue Temperature (Ts):............... 112.66667

Actual Vol. Flow Rate (acfm):.................. 184755
Dry Standard Flow Rate (dscfm):. ......•.•• 155975

Standard Flow Rate (scfm): •.••......•.•.•....... 169849



# 56Date: Project: Customer: Location: Source: 5/2/2007 M22A0346 Hibbing Taconite Hibbing, MN SV024 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: >90% Start- 7: 28 TW/RB End- 7 :37

Pressure, Barometric (Hg") : Pressure. Static(H20"): Pressure. Stack(Hg"): pitot Tube Coefficient(Cp): Duct Diameter (in): 29.86 -0.60 29.82 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas. Wet: 0.7 20.0 79.3 0.073 28.118

Moisture Determination Initial Volume •.•.•....•••• 802.086 Final Volume .••.•.•••...•.. 825.248 Meter Temperature .....••••. 50.5 Meter Delta H

•••••• 0.0 •• 2.0 Meter Volume dscf .....••••. 24.146

Traverse Delta SORT Temp. Point: (Ap) (Ap) (OF) A-l 0.58 0.7616 114 2 0.65 0.8062 114 3 0.72 0.8485 114 4 0.79 0.8888 114 5 0.87 0.9327 114 6 0.91 0.9539 114 7 0.89 0.9434 114 

### a 0.84 0.9165 114 9 0.81 0.9000 114 10 0.77 0.8775 114 11 0.65 0.8062 112 12 0.55 0.7416 110 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration...•••.•• 1. 005 Imp. # Tare Final Net

1 754.4 791.4 37.0 2 736.0 736.5 0.5 3 518.3 518.6 0.3 4 769.8 772.2 2.4 TOTAL 40.2

Traverse Delta SORT Temp. Point: (Ap) (AP) B-1 0.61 0.781 114 2 0.70 0.837 114 3 0.71 0.843 114 4 0.83 0.911 114 5 0.82 0.906 114 6 0.85 0.922 114 7 0.90 0.949 114 

### a 0.89 0.943 114 9 0.86 0.927 114 10 0.82 0.906 114 11 0.70 0.837 111 12 0.53 0.728 108

Average Delta (Ap}: ...•.•....•••. 0.7604
Average SORT Delta (Ap) : •....•••. 0.8694

Flue Gas Veloc1ty.ft/sec: •.•....• 51.617 Average Flue Temperature (Ts):............... 113.375

Actual Vol. Flow Rate (acfm): .•...•••••..•••••. 184532
Dry Standard Flow Rate (dscfm) :........... 157102

Standard Flow Rate (scfm}: •••••..•••.•..•••.•... 169434



# 57Customer: Location: Source: Hibbing Taconite Hibbing, MN SV025 Test Date: Job Number: Box Truck: Operator: 05/02107 M22A0346 Ell MBA
NO. Calibration/Bias Calculations Project: M22A0346

Date: 05/02/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 0.6 0.6 0.1 Pass Mid gas 218.1 .217.0 1.1 0.3 Pass High gas 413.0 417.4 4.4 1.1 Pass
Ispan Value: Start End Time Time Run Cma Precal Bias Postcal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 8:37 9:37 1 218.1 217.6 P 212.9 P P -0$ P "0.3 P P :1<)2:1' 104.2 -0.3 215.3 10:42 11:42 2 218.1 212.9 P 215.3 P P -0.3 P 'O} P P JOT5 109.4 0.2 214.1 11:57 12:57 3 218.1 215.3 P 216.0 P P 0.7 P <0.3 P P In3;1 114.3 0.2 215.6

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value of test Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# S8

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run 

### # System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### -0.30 -0.22 -0.30 -0.22 0.00 Upscale Gas 

### 217.60 0.15 212.93 -0.99 -1.13 2 Zero Gas 

### -0.30 -0.22 0.72 0.03 0.25 Upscale Gas 

### 212.93 -0.99 215.30 -0.41 0.57 3 Zero Gas 

### 0.72 0.03 -0.27 -0.21 -0.24 Upscale Gas 

### 215.30 -0.41 215.98 -0.25 0.16



# 59Date: Project: Customer: Location: Source: 5/2/2007 M22A0346 Hibbing Taconite Hibbing, MN SV025 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: >90% Start- 8: 48 TW/RB End- 9: 03

Pressure, Barometric (Hgll) : Pressure. Static(H20"): Pressure. Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas. Wet: 0.5 20.0 79.5 0.074 28.08 Rectangular Duct: Flue Area: inches by inches 59.583 sq. feet

Moisture Determination Initial Volume •.••.••••.•.. Final Volume .........••••.• Meter Temperature •.••.•.•.. Meter Delta H ........•.• Meter Volume dscf••.•.•...•

Traverse Delta SQRT Point: (M)**(~P)** A-l 0.62 0.7874 2 0.67 0.8185 3 0.67 0.8185 4 0.67 0.8185 5 0.67 0.8185 6 0.65 0.8062 7 0.70 0.8367 8 0.75 0.8660 9 0.77 0.8775 10 0.77 0.8775 11 0.67 0.8185 12 0.64 0.8000 825.679 848.779 53.0 2.0 23.996
Temp. (OF) 106 107 107 107 107 107 107 107 107 107 105 103 Meter Calibration.•....•.• 1. 005 Imp. # Tare Final Net

1 755.4 793.4 38.0 2 758.3 759.5 1.2 3 630.7 631.2 0.5 4 715.7 716.4 0.7 TOTAL 40.4

Traverse Delta SQRT Temp. Point:**(~P)** (M) B-1 0.63 0.794 106 2 0.65 0.806 106 3 0.67 0.819 107 4 0.67 0.819 107 5 0.68 0.825 107 6 0.67 0.819 107 7 0.73 0.854 107 8 0.67 0.819 107 9 0.66 0.812 107 10 0.65 0.806 106 11 0.60 0.775 106 12 0.47 0.686 105

Average Delta**(~P):** .•••..•.•....• 0.6667
Average SQRT Delta**(~P):** ......... 0.8157

Flue Gas Ve1ocity.ft/sec: •••••••. 48.128 Average Flue Temperature (Ts):............... 106.45833

Actual Vol. Flow Rate (acfm):.................. 172058
Dry Standard Flow Rate (dscfm) :........... 148385

Standard Flow Rate (scfm): ..••••••••.•...••••••• 160165



# 60Date: Project: Customer: Location: Source: 5/2/2007 M22A0346 Hibbing Taconite Hibbing, MN SV025 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 2 >90%

Start- 12:05 TW/RB End- 12: 13

Pressure, Barometric (Hg") : Pressure, Static(H20"): Pressure, Stack(Hg"): pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.7 19.3 80.0 0.070 28.119

Moisture Determination Initial Volume •.••.•.•.•••• 825.512 Final Volume

............... 848.577 Meter Temperature .•.•.••••. 56.0 Meter Delta H 

### ........... 2.0 Meter Volume dscf. .•.•.••.• 23.820

Traverse Delta SQRT Temp. Point: (dP) (dP) (oF) A-l 0.60 0.7746 108 2 0.60 0.7746 108 3 0.63 0.7937 107 4 0.65 0.8062 107 5 0.63 0.7937 107 6 0.70 0.8367 107 7 0.65 0.8062 107 8 0.66 0.8124 107 9 0.63 0.7937 107 10 0.65 0.8062 107 11 0.60 0.7746 105 12 0.51 0.7141 101 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration•.•••.•.• 1. 005

Imp. # Tare Final Net

1 764.4 800.9 36.5 2 695.8 696.3 0.5 3 621.5 621. 8 0.3 4 716.9 717.8 0.9 TOTAL 38.2

Traverse Delta SQRT Temp. Point: (dP) (dP) B-1 0.64 0.800 106 2 0.66 0.812 106 3 0.66 0.812 107 4 0.71 0.843 107 5 0.69 0.831 107 6 0.63 0.794 107 7 0.72 0.849 107 8 0.71 0.843 107 9 0.77 0.877 108 10 0.72 0.849 110 11 0.72 0.849 106 12 0.51 0.714 102

Average Delta (dP): •.•.•.....•..• 0.6521
Average SQRT Delta (dP): ......••• 0.8066

Flue Gas Velocity,ft/sec: ••.•.... 47.566 Average Flue Temperature (Ts):............... 106.58333

Actual Vol. Flow Rate (acfm):.................. 170048
Dry Standard Flow Rate (dscfm) :........... 147133

Standard Flow Rate (scfm): •.••••....••••.•.•..•. 158258Date: Project: Customer: Location: Source: 5/2/2007 M22A0346 Hibbing Taconite Hibbing, MN SV025 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: >90% Start- 13:24 TW/RB End- 13: 36

Pressure, Barometric (Hg") : Pressure, Static (H20") : Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.55 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.6 20.1 79.3 0.077 28.057

Moisture Determination Initial Volume ••..•.......• 849.009 Final Volume .••.....••.•.•• 872.243 Meter Temperature .••••.•.•. 69.0 Meter Delta H 

# ........... 2.0 Meter Volume dscf...•.•..•• 23.405

Traverse Delta SQRT Temp. Point: (6p) (6p) (OF) A-l 0.58 0.7616 117 2 0.64 0.8000 117 3 0.66 0.8124 110 4 0.65 0.8062 109 5 0 e •65 0.8062 108 6 0.65 0.8062 108 7 0.70 0.8367 108 8 0.69 0.8307 108 9 0.63 0.7937 107 10 0.64 0.8000 107 11 0.54 0.7348 103 12 0.51 0.7141 101 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration ...•..... 1. 005 Imp. # Tare Final Net

1 751.2 790.0 38.8 2 ·756.3 758.0 1.7 3 637.0 637.5 0.5 4 693.9 694.5 0.6 TOTAL 41. 6

Traverse Delta SQRT Temp. Point: (6p) (6p) B-1 0.58 0.762 107 2 0.62 0.787 106 3 0.66 0.812 107 4 0.63 0.794 107 5 0.69 0.831 115 6 0.64 0.800 115 7 0.66 0.812 114 8 0.62 0.787 114 9 0.73 0.854 115 10 0.73 0.854 115 11 0.69 0.831 111 12 0.60 0.775 105

Average Delta (6p): 0.6413
Average SQRT Delta (6p): 0.8001

Flue Gas Ve1oc1ty,ft/sec: .•.••••. 47.369 Average Flue Temperature (Ts):............... 109.75

Actual Vol. Flow Rate (acfm):.................. 169343
Dry Standard Flow Rate (dscfm) :........... 144590

Standard Flow Rate (scfm): •.•.••.•...••••••••... 156707



# 62Customer: Location: Source: Hibbing Taconite Hibbing, MN SV026 Test Date: Job Number: Box Truck: Operator: 5/2 - 05/3/2007 M22A0346 E1l MBA
NO. Calibration/Bias Calculations Project: M22A0346

Date: 5/2 - 05/3/2007
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 0.6 0.6 0.1 Pass Mid gas 218.1 217.0 1.1 0.3 Pass High gas 413.0 417.4 4.4 1.1 Pass

### ~span Value: Start End Time Time Run Cma Precal Bias Postcal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 13:11 14:11 1 218.1 216.0 P 216.8 P P ; ;0.3 P -0,3 P P 104.3 105.3 -0.3 216.4 14:32 15:32 2 218.1 216.8 P 220.9 P P -0.3 P ,0.3 P P 104;9 104.7 -0.3 218.8 5:45 6:45 3 218.1 213.9 P 216.0 P P -0.4 P '0.0 P P 98;9 100.5 -0.2 214.9

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value oltest Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 63

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run 

### # System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### -0.26 -0.21 -0.30 -0.22 -0.01 Upscale Gas 

### 215.98 -0.25 216.80 -0.05 0.20 2 Zero Gas 

### -0.30 -0.22 -0.30 -0.22 0.00 Upscale Gas 

### 216.80 -0.05 220.86 0.93 0.98 3 Zero Gas 

### -0.36 -0.23 0.00 -0.15 0.09 Upscale Gas 

### 213.87 -0.76 216.00 -0.24 0.52



# 64Date: Project: Customer: Location: Source: 5/2/2007 M22A0346 Hibbing Taconite Hibbing, MN SV026 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 1 >90 ...

Start- 13:53 TW/RB End- 14: 10

Pressure, Barometric(Hg"): Pressure. Static (H20") : Pressure. Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(\): Oxygen Content(\): Nitrogen Content(\): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas. Wet: 0.5 20.0 79.5 0.062 28.21 Rectangular Duct: Flue Area: inches by inches 59.583 sq. feet

Moisture Determination Initial Vo1wne •••.••••.•..• Final Vo1wne

. Meter Temperature•.•.•.•.•. Meter Delta H .••..•.•... Meter Vo1wne dscf ........••

Traverse Delta SQRT Point: (6p) (6p) A-1 0.55 0.7416 2 0.64 0.8000 3 0.71 0.8426 4 0.73 0.8544 5 0.80 0.8944 6 0.87 0.9327 7 0.81 0.9000 8 0.85 0.9220 9 0.79 0.8888 10 0.80 0.8944 11 0.73 0.8544 12 0.50 0.7071 872.417 895.886 61. 0 2.0 24.005
Temp. (oF) 102 103 102 102 102 102 99 101 102 102 100 98 Meter Calibration ......••• 1. 005 Imp. # Tare Final Net

1 791.4 822.8 31.4 2 736.5 737.5 1.0 3 518.6 518.7 0.1 4 772.7 773.8 1.1 TOTAL 33.6

Traverse Delta SQRT Temp. Point: (6p) (6p) B-1 0.55 0.742 107 2 0.57 0.755 106 3 0.64 0.800 107 4 0.68 0.825 107 5 0.75 0.866 107 6 0.70 0.837 106 7 0.83 0.911 106 8 0.84 0.917 104 9 0.95 0.975 104 10 0.91 0.954 104 11 0.91 0.954 104 12 0.84 0.917 98

Average Delta (6p): 0.7479
Average SQRT Delta (6p): ••••••••• 0.8618

Flue Gas Ve1ocity.ft/sec: •••••••. 50.586 Average Flue Temperature (Ts):............... 103.125

Actual Vol. Flow Rate (acfm):.................. 180846
Dry Standard Flow Rate (dscfm) :........... 158858

Standard Flow Rate (scfm): •...••......••.•..•... 169342



# 65Date: Project: Customer: Location: Source: 5/2/2007 M22A0346 Hibbing Taconite Hibbing, MN SV026 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 2 >90%

Start- 15:07 TW/RB End- 15: 16

Pressure, Barometric (Hg") : Pressure. Static(H20"): Pressure. Stack(Hg"): pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.7 19.3 80.0 0.066 28.170

Moisture Determination Initial Volume ••.•...•.••.. 896.368 Final Volume •..•........•.. 919.845 Meter Temperature .........• 60.0 Meter Delta H • 0 ••••••••• 2.0 Meter Volume dscf .••....... 24.059

Traverse Delta SQRT Temp. Point: (tip) (tip) (OF) A-1 0.54 0.7348 101 2 0.64 0.8000 101 3 0.70 0.8367 101 4 0.75 0.8660 102 5 0.74 0.8602 101 6 0.75 0.8660 101 7 0.78 0.8832 101 8 0.78 0.8832 102 9 0.74 0.8602 102 10 0.79 0.8888 102 11 0.79 0.8888 102 12 0.65 0.8062 99 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration ...•..... 1. 005

Imp. # Tare Final Net

1 800.9 834.6 33.7 2 696.3 696.6 0.3 3 621. 8 622.9 1.1 4 717.8 718.5 0.7 TOTAL 35.8

Traverse Delta SQRT Temp. Point: (tip) (tip) B-1 0.42 0.648 102 2 0.50 0.707 104 3 0.54 0.735 102 4 0.60 0.775 101 5 0.68 0.825 101 6 0.72 0.849 101 7 0.90 0.949 101 8 0.89 0.943 101 9 0.87 0.933 102 10 0.93 0.964 101 11 0.99 0.995 101 12 0.89 0.943 98

Average Delta (tiP): 0.7325
Average SQRT Delta (tiP): ..•.•.••• 0.8516

Flue Gas Ve1ocity,ft/sec: ••••.•.• 49.939 Average Flue Temperature (Ts):............... 101.25

Actual Vol. Flow Rate (acfm):.................. 178533
Dry Standard Flow Rate (dscfm) :........... 156739

Standard Flow Rate (scfm): •.•••••••.....••.••••. 167735



# 66Date: Project: Customer: Location: Source: 5/3/2007 M22A0346 Hibbing Taconite Hibbing, MN SV026 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 3 >90%

Start- 7:10 TW/RB End- 7: 17

Pressure, Barometric (Hgn) : Pressure, Static (H20 n) : Pressure, Stack(Hgn): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.60 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.6 20.1 79.3 0.059 28.262

Moisture Determination Initial Volume .•.•......... 920.027 Final Volume •..•.•••••.•.•. 942.395 Meter Temperature ••..•..... 42.5 Meter Delta H 

## ........... 2.0 Meter Volume dscf

.......... 23.721

Traverse Delta SORT Temp. Point: (8P) (8P) (oF) A-1 0.61 0.7810 104 2 0.66 0.8124 104 3 0.72 0.8485 104 4 0.79 0.8888 104 5 0.79 0.8888 104 6 0.79 0.8888 104 7 0.85 0.9220 104 8 0.83 0.9110 104 9 0.82 0.9055 103 10 0.82 0.9055 102 11 0.72 0.8485 101 12 0.58 0.7616 98 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration••••••••• 1.005 Imp. # Tare Final Net

1 790.0 822.2 32 .2 2 758.0 757.9 -0.1 3 637.5 637.7 0.2 4 694.5 693.5 -1. 0 TOTAL 31.3

Traverse Delta SORT Temp. Point: (8P) (8P) B-1 0.61 0.781 104 2 0.67 0.819 104 3 0.71 0.843 104 4 0.83 0.911 104 5 0.82 0.906 104 6 0.83 0.911 104 7 1. 30 1.140 100 8 1.10 1. 049 99 9 1.10 1.049 99 10 1.10 1. 049 99 11 0.98 0.990 97 12 0.85 0.922 95

Average Delta (8P): ....•••••••.•• 0.8283
Average SORT Delta (8P) : ...•.•.•. 0.9055

Flue Gas Ve1oc1ty,ft/sec: •.....•• 53.052 Average Flue Temperature (Ts):............... 102.04167

Actual Vol. Flow Rate (acfm):.................. 189663
Dry Standard Flow Rate (dscfm) :........... 167478

Standard Flow Rate (scfm): .....••••••••••••.••.. 177897



# 67Customer: Location: Source: Hibbing Taconite Hibbing, MN SV027 Test Date: Job Number: Box Truck: Operator: 05/03/07 M22A0346 E11 MBA
NOx Calibration/Bias Calculations Project: M22A0346

Date: 05/03/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 "0.6 0.6 0.1 Pass Mid gas 218.1 217.0 1.1 0.3 Pass High gas 413.0 417'.4 4.4 1.1 Pass
Ispan Value: Start End Time Time Run Cma Preeal Bias Posteal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 7:01 8:01 1 218.1 216.0 P 216.1 P P 0;1 P 

### o.s P P 67.5: 67.8 0.5 216.1 8:13 9:13 2 218.1 216.1 P 213.9 P P 0.9 P -0:3 P P 61.0, 67.8 0.3 215.0 9:33 10:33 3 218.1 213.9 P 214.1 P P -0.4 P ·0.3 P P 67;2 68.7 -0.3 214.0

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value of test Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 68

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run# System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### 0.09 -0.12 0.90 0.07 0.20 Upscale Gas 

### 216.03 -0.23 216.10 -0.22 0.02 2 Zero Gas 

### 0.90 0.07 -0.30 -0.22 -0.29 Upscale Gas 

### 216.10 -0.22 213.88 -0.76 -0.54 3 Zero Gas 

### -0.36 -0.23 -0.32 -0.22 0.01 Upscale Gas 

### 213.87 -0.76 214.11 -0.70 0.06



# 69Date: Project: Customer: Location:

source: 5/3/2007 M22A0346 Hibbing Taconite Hibbing, MN SV027 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By:**~90%** Start- 7:42 TW/RB End- 7:50

Pressure, Barometric (Hg") : Pressure, Static (H20") : Pressure, Stack(Hg"): pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 20.0 79.5 0.068 28.14 Rectangular Duct: Flue Area:

Moisture Determination Initial Volume .....•.••.•.. Final Volume ....•.••.••.... Meter Temperature .....•.•.• Meter Delta H .....•.••.• Meter Volume dscf.•.....•.•

Traverse Delta SQRT Point: (Ap) (Ap) A-1 0.49 0.7000 2 0.65 0.8062 3 0.74 0.8602 4 0.76 0.8718 5 0.77 0.8775 6 0.81 0.9000 7 0.96 0.9798 8 0.97 0.9849 9 0.96 0.9798 10 0.92 0.9592 11 0.83 0.9110 12 0.72 0.8485 inches by 59.583

942.875 964.787 49.5 2.0 22.918
Temp. (OF) 96 96 96 96 96 96 96 96 96 96 95 91 inches sq. feet

Meter Calibration•...••.•• 1.005

Imp. # Tare Final Net

1 822.8 856.0 33.2 2 737.5 737.5 0.0 3 518.7 519.1 0.4 4 773.8 775.5 1.7 TOTAL 35.3

Traverse Delta SQRT Temp. Point: (Ap) (Ap) B-1 0.57 0.755 96 2 0.67 0.700 96 3 0.70 0.837 96 4 0.80 0.894 97 5 0.82 0.906 96 6 0.85 0.922 96 7 0.95 0.975 96 8 0.89 0.943 97 9 0.94 0.970 97 10 0.92 0.959 97 11 0.85 0.922 95 12 0.64 0.800 92

Average Delta (Ap): •....•••••..•. 0.7992
Average SQRT Delta (Ap): ...•••.•. 0.8859

Flue Gas Ve1ocity,ft/sec: .•...••• 51.714 Average Flue Temperature (Ts):............... 95.708333

Actual Vol. Flow Rate (acfm):.................. 184879
Dry Standard Flow Rate (dscfm) :........... 163553

Standard Flow Rate (scfm): .•....••••••....•••••• 175431



# 70Date: Project: Customer: Location: Source: 5(3(2007 M22A0346 Hibbing Taconite Hibbing, MN SV027 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 2 >90%

Start- 8:43 TW(RB End- 8:49

Pressure, Barometric (Hg") : Pressure. Static(H20"): Pressure. Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas. Wet: 0.5 20.0 79.5 0.065 28.169

Moisture Determination Init ial Volume ...•..•.••.•• 964.880 Final Volume .•.•.•..•.•.... 988.213 Meter Temperature ..••.•••.• 55.0 Meter Delta H 

## ........... 2.0 Meter Volume dscf

.......... 24.144

Traverse Delta SORT Temp. Point: (Ap) (Ap) (OF) A-l 0.58 0.7616 97 2 0.67 0.8185 97 3 0.74 0.8602 97 4 0.78 0.8832 97 5 0.81 0.9000 97 6 0.85 0.9220 97 7 0.85 0.9220 97 8 0.89 0.9434 97 9 0.86 0.9274 97 10 0.87 0.9327 97 11 0.73 0.8544 95 12 0.62 0.7874 92 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration••••..•.• 1.005 Imp. # Tare Final Net

1 729.8 763.0 33.2 2 737.5 738.2 0.7 3 519.1 519.3 0.2 4 775.5 777.2 1.7 TOTAL 35.8

Traverse Delta SORT Temp. Point: (Ap) (AP) B-1 0.49 0.700 96 2 0.63 0.794 97 3 0.66 0.812 97 4 0.73 0.854 97 5 0.74 0.860 97 6 0.80 0.894 97 7 0.90 0.949 97 8 1.10 1. 049 97 9 1. 00 1.000 97 10 0.98 0.990 97 11 0.89 0.943 94 12 0.64 0.800 90

Average Delta (Ap): •••••••••••••• 0.7838
Average SORT Delta (Ap) : ••••••••• 0.8816

Flue Gas Velocity.ft/sec: ...••••. 51.467 Average Flue Temperature (Ts):............... 96.25

Actual Vol. Flow Rate (acfm)'.................. 183993
Dry Standard Flow Rate (dscfm) :........... 163023

Standard Flow Rate (scfm): •.•.....•••••••••.•.•. 174420



# 71.PITOT TRAVERSE DATA

Date: 5/3/2007 Traverse Number: 3 Project: M22A0346 Condition: >90% Customer: Hibbing Taconite Time: Start- 9:47 End- 10:07 Location: Hibbing, MN Data Taken By: TW/RB Source: SV027

Pressure, Barometric (Hg") : Pressure, Static(H20"): Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content('): Oxygen Content('): Nitrogen Content('): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.4 20.0 79.6 0.066 28.143 Rectangular Duct: Flue Area: 0.00 inches by 0.00 inches 59.583 sq. feet

Moisture Determination Initial Volume ............. 988.506 Final Volume ............... 1011.638 Meter Temperature4 .......... 53.0 Meter Delta H 

### ................. 2.0 Meter Volume dscf.......... 24.029

Traverse Delta SQRT Temp. Point: (Ap) (Ap) (OF) A-I 0.63 0.7937 98 2 0.69 0.8307 98 3 0.75 0.8660 98 4 0.79 0.8888 98 5 0.88 0.9381 98 6 0.91 0.9539 98 7 0.88 0.9381 98 8 0.86 0.9274 98 9 0.87 0.9327 98 10 0.89 0.9434 98 11 0.80 0.8944 98 12 0.66 0.8124 96

Average Delta (Ap): .•••.•.••••••• 0.7700
Average SQRT Delta (Ap) : •..•••••• 0.8742

Flue Gas Veloc1ty,ft/sec: 51.113 Meter Calibration ......... 1. 005 Imp. # Tare Final Net

1 834.6 868.4 33.8 2 696.6 697.4 0.8 3 622.9 623.9 1.0 4 718.5 719.1 0.6 TOTAL 36.2

Traverse Delta SQRT Temp. Point: (Ap) (Ap) B-1 0.56 0.748 97 2 0.64 0.800 98 3 0.70 0.837 98 4 0.73 0.854 98 5 0.78 0.883 98 6 0.82 0.906 98 7 0.84 0.917 98 8 0.92 0.959 98 9 0.89 0.943 98 10 0.86 0.927 97 11 0.73 0.854 95 12 0.40 0.632 92

Average Flue Temperature (Ts):............... 97.458333

Actual Vol. Flow Rate (acfm):.................. 182729
Dry Standard Flow Rate (dscfm) :........... 161383

Standard Flow Rate (scfm): 172847



# 72Customer: Location: Source: Hibbing Taconite Hibbing, MN SV028 Test Date: Job Number: Box Truck: Operator: 05/03107 M22A0346 E11 MBA
NOx Calibration/Bias Calculations Project: M22A0346

Date: 05/03/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 0.6 0.6 0.1 Pass Mid gas 218.1 ,217.0 1.1 0.3 Pass High gas 413.0 417.4 4.4 1.1 Pass
IS pan Value: Start End Time Time Run Cma Precal Bias Postcal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 10:54 11:54 1 218.1 214.1 P '216.9 ", P P ·-0.3, P .0.4. P P

" 52:0 52.6 0.1 215.5 12:10 13:10 2 218.1 216.9 P 218.0 ' P P 0.4 P -0.3 P P ,'52:2 52.3 0.1 217.5 13:26 14:26 3 218.1 213.9 P 217.9 P P -0.4 P -0.3 P P 53:0 53.8 -0.3 215.9

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value of test Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 73

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run 

### # System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### -0.30 -0.22 0.40 -0.05 0.17 Upscale Gas 

### 214.10 -0.70 216.94 -0.01 0.69 2 Zero Gas 

### 0.40 -0.05 -0.30 -0.22 -0.17 Upscale Gas 

### 216.94 -0.01 217.96 0.23 0.25 3 Zero Gas 

### -0.36 -0.23 -0.29 -0.22 0.02 Upscale Gas 

### 213.87 -0.76 217.91 0.22 0.98



# 74Date: Project: Customer: Location: Source: 5/3/2007 M22A0346 Hibbing Taconite Hibbing, MN SV028 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: >90 .. Start- 11: 37 TW/RB End- 11:40

Pressure, Barometric (Hg") : Pressure, Static (H20") : Pressure, Stack(Hg"): pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(\): Oxygen Content(\): Nitrogen Content(\): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 20.0 79.5 0.064 28.18 Rectangular Duct: Flue Area:

Moisture Determination Initial Volume •.....•.•.••• Final Volume

. Meter Temperature •.•....... Meter Delta H •.......... Meter Volume dscf•••.•.•••.

Traverse Delta SQRT Point: (Ap) (Ap) A-l 0.84 0.9165 2 0.84 0.9165 3 0.87 0.9327 4 0.86 0.9274 5 0.83 0.9110 6 0.86 0.9274 7 0.99 0.9950 8 1. 00 1. 0000 9 1.10 1. 0488 10 1. 00 1. 0000 11 0.97 0.9849 12 0.73 0.8544 inches by 59.583

12.014 35.229 62.0 2.0 23.700
Temp. (oF) 89 89 89 89 89 89 89 89 89 89 89 83 inches sq. feet

Meter Calibration•.•.•.•.• 1. 005

Imp. # Tare Final Net

1 763.0 794.9 31. 9 2 738.2 739.4 1.2 3 519.3 519.9 0.6 4 777.2 778.1 0.9 TOTAL 34.6

Traverse Delta SQRT Temp. Point: (Ap) (Ap) B-1 0.74 0.860 89 2 0,92 0.700 89 3 0.93 0.964 89 4 0.90 0.949 89 5 0.86 0.927 89 6 0.85 0.922 89 7 0.85 0.922 89 8 0.90 0.949 89 9 0.90 0.949 89 10 0.90 0.949 89 11 0.99 0.995 89 12 0.87 0.933 89 89
Average Delta (Ap): .•.....•••••.• 0.8958
Average SQRT Delta (Ap): .....•••• 0.9347

Flue Gas Velocity,ft/sec: .•.•••.. 54.187 Average Flue Temperature (Ts):............... 88.75

Actual Vol. Flow Rate (acfm):.................. 193718
Dry Standard Flow Rate (dscfm) :........... 174162

Standard Flow Rate (scfm): •••.•••.•.••••••.•.•.. 186150



# 75Date, Project, Customer: Location, Source: 5/3/2007 M22A0346 Hibbing Taconite Hibbing, MN SV028 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 2 >90%

Start- 12:55 TW/RB End- 13: 05

Pressure, Barometric (Hg") : Pressure, Static (H20") : Pressure, Stack(Hg")' Pitot Tube Coefficient (Cp) : Duct Diameter (in), 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%), Nitrogen Content(%): Water Vapor in Flue Gas (Bws) , Molecular Wt. of Gas, Wet, 0.5 20.0 79.5 0.063 28.196

Moisture Determination Initial Volume •..••.••••••. 35.864 Final Volume .•............. 59.474 Meter Temperature .......... 65.0 Meter Delta H 

## ........... 2.0 Meter Volume dscf••..•.•... 23.965

Traverse Delta SQRT Temp. Point: (tip) (tip) (oF) A-1 0.81 0.9000 90 2 0.89 0.9434 90 3 0.87 0.9327 90 4 0.84 0.9165 90 5 0.83 0.9110 90 6 0.82 0.9055 90 7 0.93 0.9644 90 8 0.91 0.9539 90 9 0.95 0.9747 90 10 0.99 0.9950 90 11 0.88 0.9381 88 12 0.81 0.9000 86 Rectangular Duct, Flue Area, 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration ...•....• 1. 005

Imp. # Tare Final Net

1 794.9 815.8 20.9 2 739.4 751.4 12.0 3 519.9 520.5 0.6 4 778.1 778.7 0.6 TOTAL 34.1

Traverse Delta SQRT Temp. Point: (tip) (tiP) B-1 0.87 0.933 91 2 0.90 0.949 92 3 0.91 0.954 92 4 0.90 0.949 92 5 0.88 0.938 92 6 0.82 0.906 92 7 0.86 0.927 92 8 0.87 0.933 91 9 0.87 0.933 91 10 0.92 0.959 91 11 0.95 0.975 90 12 0.92 0.959 87

Average Delta (tiP): •••••••••••••• 0.8833
Average SQRT Delta (tiP): •.••.••.. 0.9395

Flue Gas Ve1ocity,ft/sec: •.•.••.. 54.527 Average Flue Temperature (Ts):............... 90.291667

Actual Vol. Flow Rate (acfm) : •••.••.•••...••.•• 194934
Dry Standard Flow Rate (dscfm) :........... 175050

Standard Flow Rate (scfm): ..•••••••••..•........ 186794



# 76Date: Project: Customer: Location: Source: 5/3/2007 M22A0346 Hibbing Taconite Hibbing, MN SV028 PITOT TRAVERSE DATA

Traverse Nwnber: Condition: Time: Data Taken By: >90% Start- 13: 51 TW/RB End- 13: 58

Pressure, Barometric (HgU) : Pressure, Static (H20U) : Pressure, Stack(HgU): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.90 -0.50 29.86 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bwe): Molecular Wt. of Gas. Wet: 0.5 20.0 79.5 0.059 28.240

Moisture Determination Initial Volume ...•.••.••.•• 59.876 Final Volume •••.••..•.••... 83.186 Meter Temperature ..•...•.•. 68.0 Meter Delta H 

## ........... 2.0 Meter Volume dscf........•. 23.526

Traverse Delta SORT Temp. Point: (Ap) (Ap) (oF) A-I 0.86 0.9274 93 2 0.84 0.9165 93 3 0.85 0.9220 93 4 0.86 0.9274 93 5 0.82 0.9055 93 6 0.83 0.9110 93 7 0.93 0.9644 93 8 0.94 0.9695 93 9 0.91 0.9539 93 10 0.91 0.9539 93 11 0.91 0.9539 90 12 0.80 0.8944 87 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration .•....... 1.005 Imp. # Tare Final Net

1 868.4 897.2 28.8 2 697 .4 698.8 1.4 3 623.9 625.2 1.3 4 719.1 718.8 -0.3 TOTAL 31.2

Traverse Delta SORT Temp. Point: (Ap) (Ap) B-1 0.89 0.943 93 2 0.98 0.990 93 3 0.94 0.970 93 4 0.91 0.954 92 5 0.84 0.917 92 6 0.83 0.911 92 7 0.83 0.911 92 8 0.85 0.922 92 9 0.84 0.917 92 10 0.87 0.933 92 11 0.97 0.985 88 12 0.94 0.970 86

Average Delta (Ap): .••••.••...... 0.8813
Average SORT Delta (AP) : ••••••••• 0.9384

Flue Gas Velocity.ft/sec: .••••••. 54.494 Average Flue Temperature (Ts):............... 91.833333

Actual Vol. Flow Rate (acfm):.................. 194815
Dry Standard Flow Rate (dscfm) :........... 175203

Standard Flow Rate (scfm): ..•.....••.•..•.•...•. 186158



# 77Customer: Location: Source: Hibbing Taconite Hibbing, MN SV029 Test Date: Job Number: Box Truck: Operator: 05/08/07 M22A0346 E11 MBA NOx Calibration/Bias Calculations Project: M22A0346

Date: 05/08/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 0.7 0.7 0.2 Pass Mid gas 218.1 215.6 2.5 0.6 Pass High gas 413.0 412.6 0.4 0.1 Pass
Ispan Value: Start End Time Time Run Cma Precal Bias Postcat Bias Drift Pre zero Bias Post zero Bias Drift C Caas Co Cm 10:52 11:52 1 218.1·. 219.0 P 222.3 P P 0.6 P 0,7,· ' P P 34.7 33.8 0.6 220.6 12:02 13:02 2 221.4 222.3 P 222.5 P P 0.7 P 0.7. P P 33.2 32.4 0.7 222.4 13:12 14:12 3 218.1 217.4 P 220.2 P P 1.7 P O:L P P ,.' 31:9 30.8 1.2 218.8

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value of test Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 78

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run# System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### 0.64 -0.01 0.65 0.00 0.00 Upscale Gas 

### 218.97 0.83 222.25 1.62 0.79 2 Zero Gas 

### 0.65 0.00 0.66 0.00 0.00 Upscale Gas 

### 222.25 1.62 222.48 1.68 0.05 3 Zero Gas 

### 1.66 0.24 0.67 0.00 -0.24 Upscale Gas 

### 217.43 0.45 220.20 1.13 0.67



# 79Date: Project: Customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV029 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 1 >90%

Start- 11:23 TW/RB End- 11:32

Pressure, Barometric (Hgll) : Pressure, Static (H20") : Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 -0.66 29.55 0.840 104.52 Carbon Dioxide Content(\): Oxygen Content(\) : Nitrogen Content(\): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 19.0 80.5 0.078 28.00 Rectangular Duct: Flue Area: inches by inches 59.583 sq. feet

Moisture Determination Initial Volume •••..••••••.• Final Volume ...•..........• Meter Temperature ..•..•••.• Meter Delta H ...•....... Meter Volume dscf•.••.•.•.•

Traverse Delta SORT Point: (Ap) (Ap) A-1 0.87 0.9327 2 0.87 0.9327 3 0.92 0.9592 4 1.00 1.0000 5 0.99 0.9950 I; 1.10 1.0488 7 0.99 0.9950 8 0.98 0.9899 9 0.94 0.9695 10 0.91 0.9539 11 0.84 0.9165 12 0.74 0.8602 269.883 294.417 91.0 2.0 23.491
Temp. (oF) 98 98 98 98 98 98 98 98 98 97 96 97 Meter Calibration•...•.... 1. 005 Imp. # Tare Final Net

1 808.6 843.1 34.5 2 703.6 706.7 3.1 3 622.1 623.6 1.5 4 645.6 648.4 2.8 TOTAL 41. 9

Traverse Delta SORT Temp. Point: (Ap) (Ap) B-1 0.. 86 0.927 96 2 0.96 0.980 96 3 0.98 0.990 97 4 1. 00 1.000 97 5 0.99 0.995 97 I; 1.00 1.000 98 7 1.00 1.000 97 8 0.95 0.975 97 9 0.93 0.964 97 10 0.93 0.964 97 11 0.86 0.927 97 12 0.73 0.854 87

Average Delta (Ap): .....•••••.•.. 0.9308
Average SORT Delta (Ap): ..•••••.• 0.9638

Flue Gas Ve1ocity,ft/sec: .•.••••• 56.763 Average Flue Temperature (Ts):............... 96.875

Actual Vol. Flow Rate (acfm):.................. 202928
Dry Standard Flow Rate (dscfm) :........... 175397

Standard Flow Rate (scfm): ..•..•••••.•••...•..•. 190147



# 80Date: Project: Customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV029 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 2 >90%

Start- 12:44 TW/RB End- 12: 53

Pressure, Barometric (Hgn) : Pressure, Static(H20n): Pressure, Stack(Hgn), Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%), Nitrogen Content(%): Water Vapor in Flue Gas (Bws) , Molecular Wt. of Gas, Wet, 0.5 19.0 80.5 0.097 27.793 Rectangular Duct: Flue Area: 0.00 inches by 0.00 inches 59.583 sq. feet

Moisture Determination Initial Volume •••••.•.••.•• 294.747 Final Volume ..•...•....•.•. 319.211 Meter Temperature•••••••••• 94.0 Meter Delta H 

### ........... 2.0 Meter Volume dscf••••.••••. 23.297

Traverse Delta SQRT Temp. Point:**(~P) (~P)**  (OF) A-1 0.88 0.9381 100 2 1. 00 1. 0000 99 3 1. 00 1. 0000 99 4 1.10 1. 0488 99 5 1.10 1. 0488 99 6 1.00 1.0000 99 7 1.00 1.0000 99 8 1. 00 1. 0000 99 9 1.00 1. 0000 99 10 0.91 0.9539 99 11 0.84 0.9165 99 12 0.73 0.8544 96 Meter Calibration.••••••.. 1.005 Imp. # Tare Final Net

1 753.6 796.5 42.9 2 759.6 763.1 3.5 3 518.7 519.9 1.2 4 778.7 783.9 5.2 TOTAL 52.8

Traverse Delta SQRT Temp. Point,**(~P) (~P)**  B-1 0.91 0.954 100 2 0.92 0.959 100 3 0.99 0.995 100 4 1.00 1. 000 99 5 1.10 1.049 99 6 1.10 1. 049 99 7 1. 00 1. 000 99 8 0.99 0.995 99 9 0.96 0.980 98 10 0.93 0.964 98 11 0.85 0.922 97 12 0.79 0.889 88

Average Delta**(~P):** •...•.•••••••. 0.9625 Average Flue Temperature (Ts): •••..••..•..... 98.416667
Average SQRT Delta**(~P)** : ..•.•.••• 0.9798 Actual Vol. Flow Rate (acfm):.................. 207393

Flue Gas Ve1oc1ty,ft/sec: .••..•.• 58.012 Dry Standard Flow Rate (dscfm) : ••••••..••. 175024

Standard Flow Rate \scfm): ......•.••..••.•....•. 193727



# 81Date: Project: Customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV029 PITOT TRAVERSE DATA

Traverse Number: Condition, Time: Data Taken By: >90% Start

- 13: 12 TW/RB End- 13:20

Pressure. Barometric (Hg") : Pressure. Static (H20") : Pressure. Stack(Hg"): pitot Tube Coefficient (Cp) : Duct Diameter (in), 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(\), Oxygen Content(\): Nitrogen Content(\), Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 19.0 80.5 0.074 28.040 Rectangular Duct, Flue Area: 0.00 inches by 0.00 inches 59.583 sq. feet

Moisture Determination Initial Volume ...•......... 319.447 Final Volume •.•••••••.••••. 343.778 Meter Temperature ••••.•.••. 89.0 Meter Delta H 

## ........... 2.0 Meter Volume dscf•.•..•.•.• 23.381

Traverse Delta SQRT Temp. Point: (,1,p) (,1,p) (oF) A-1 0.79 0.8888 97 2 0.98 0.9899 97 3 1.10 1.0488 97 4 1.10 1. 0488 97 5 1.20 1.0954 98 6 1.20 1.0954 98 7 1.10 1. 0488 99 B 1. 00 1. 0000 99 9 0.94 0.9695 99 10 0.94 0.9695 99 11 0,83 0.9110 99 12 0.75 0.8660 92

Average Delta (,1,P): 0.9838
Average SQRT Delta (,1,P), ••.•.•... 0.9897

Flue Gas Ve1ocity.ft/sec: •.....•. 58.286 Meter Calibration•..•.•..• 1. 005 Imp. # Tare Final Net

1 684.8 715.7 30.9 2 706.7 711.7 5.0 3 623.6 624.9 1.3 4 648.4 650.7 2.3 39.5

Traverse Delta SQRT Temp. Point, (,1,p) (,1,p) B-1 0.77 0.877 97 2 0.93 0.964 97 3 cO•95 0.975 97 4 1.10 1. 049 97 5 1.10 1.049 98 6 1.10 1.049 98 7 0.99 0.995 98 B 1.10 1.049 97 9 0.98 0.990 97 10 0.93 0.964 97 11 0.87 0.933 97 12 0.86 0.927 97

Average Flue Temperature (Ts):............... 97.416667

Actual Vol. Flow Rate (acfm)' ••••••••••.•.•..•• 208374
Dry Standard Flow Rate (dscfm) :........... 180607

Standard Flow Rate (scfmJ: •••.•••.•.••.•...••••• 194993



# 82Customer: Location: Source: Hibbing Taconite Hibbing, MN SV030 Test Date: Job Number: Box Truck: Operator: 05/08/07 M22A0346 E11 MBA 

### NOx 

### CalibrationlBias Calculations Project: M22A0346

Date: 05/08/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 0.7 0.7 0.2 Pass Mid gas 218.1 215.6 2.5 0.6 Pass High gas 413.0 412.6 0.4 0.1 Pass
Ispan Value: Start End Time Time Run Cma Preeal Bias PosteaI Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 7:08 8:08 1 218.1 217.7. P 217.7 P P 0,7. P I···.
··..0.7 P P k**47:3~** 46.8 0.7 217.7 8:19 9:19 2 218.1 217.7 P I· 217.9 P P 0.7 P liO:6 P P 47:5 47.0 0.7 217.8 9:32 10:32 3 218.1 217.4 P 219,0 P P 1.7 P 0.6 P P 

### :49:6 48.7 1.2 218.2

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value ottest Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 83

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run# System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### 0.66 0.00 0.66 0.00 0.00 Upscale Gas 

### 217.70 0.52 217.70 0.52 0.00 2 Zero Gas 

### 0.66 0.00 0.64 -0.01 0.00 Upscale Gas 

### 217.70 0.52 217.93 0.58 0.06 3 Zero Gas 

### 1.66 0.24 0.65 -0.01 -0.24 Upscale Gas 

### 217.43 0.45 218.97 0.83 0.37



# 84Date: Project: Customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV030 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: >90% Start- 7:26 TW/RB End- 7:35

Pressure, Barometric (Hgtl) : Pressure, Static (H20") : Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(\): Oxygen Content(\): Nitrogen Content(\): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.6 19.0 80.4 0.082 27.97 Rectangular Duct: Flue Area:

Moisture Determination Initia1 Volume .......•..•.• Final Volume .••••••...•••.• Meter Temperature .•.••••.•• Meter Delta H •.•.•.••.•. Meter Volume dscf••.••••.•.

Traverse Delta SORT Point: (6p) (6p) A-1 0.90 0.9487 2 0.85 0.9220 3 0.98 0.9899 4 1.10 1. 0488 5 1.10 1.0488 6 1.20 1.0954 7 1.10 1.0488 8 1. 00 1. 0000 9 0.99 0.9950 10 0.95 0.9747 11 0.90 0.9487 12 0.88 0.9381 inches by 59.583

195.719 219.929 80.0 2.0 23.653
Temp. (oF) 102 102 102 102 102 102 102 102 102 103 103 93 inches sq. feet

Meter Calibration•.•••.••• 1.005 Imp. # Tare Final Net

1 734.7 770.1 35.4 2 698.3 700.8 2.5 3 619.4 621.2 1.8 4 637.6 642.5 4.9 TOTAL 44.6

Traverse Delta SORT Temp. Point: (6p) (6p) B-1 .0.88 0.938 103 2 0.87 0.700 102 3 0.95 0.975 102 4 1. 00 1. 000 102 5 1.00 1.000 103 6 1.00 1. 000 103 7 1. 00 1. 000 102 8 1. 00 1. 000 102 9 0.99 0.995 102 10 1.10 1.049 102 11 0.97 0.985 102 12 0.84 0.917 91

Average Delta (6p): 0.9813 Average Flue Temperature (Ts) : •••..•••••••••. 101.375
Average SORT Delta (6Pj : .•....... 0.9799 Actual Vol. Flow Rate (acfm):.................. 207291

Flue Gas Ve1ocity,ft/sec: •.••••.• 57.983 Dry Standard Flow Rate (dscfm) : .•.•.•.•... 176885

Standard Flow Rate (scfm): •••••••••••.......•.•. 192611



# 85Date: Project: Customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV030 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 2 >90%

Start- 7: 45 TW/RB End- 7:56

Pressure, Barometric (HgU) : Pressure, Static (H20") : Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 19.0 80.5 0.084 27.933

Moisture Determination Initial Volume ....•••.••••. 171. 352 Pinal Volume ••.•••.••.•.... 195.462 Meter Temperature .......... 84.0 Meter Delta H

• _0 •••••••• 2.0 Meter Volume dscf ...•.••••. 23.382

Traverse Delta SQRT Temp. Point: (.1.P) (.1.p) (Op) A-1 0.79 0.8888 101 2 0.80 0.8944 102 3 1.00 1.0000 101 4 1.10 1. 0488 102 5 1.20 1.0954 102 6 1.10 1.0488 102 7 1. 00 1.0000 102 8 1.10 1. 0488 102 9 1. 00 1.0000 102 10 0.98 0.9899 102 11 0.90 0.9487 102 12 0.89 0.9434 96 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration•••.••••. 1.005

Imp. # Tare Pinal Net

1 770.1 808.6 38.5 2 700.8 703.6 2.8 3 621. 2 622.1 0.9 4 642.5 645.6 3.1 TOTAL 45.3

Traverse Delta SQRT Temp. Point: (.1.P) (.1.p) B-1 0.88 0.938 102 2 0.91 0.954 102 3 0.93 0.964 102 4 1. 00 1.000 102 5 0.96 0.980 103 6 1. 00 1. 000 103 7 1. 00 1.000 103 8 0.98 0.990 103 9 0.95 0.975 102 10 0.93 0.964 102 11 0.88 0.938 102 12 0.85 0.922 96

Average Delta (.1.P): •••....•••••.• 0.9638
Average SQRT Delta (.1.P): ...•••.•• 0.9805

P1ue Gas Ve1ocity,ft/sec: .•...•.• 58.071 Average P1ue Temperature (Ts):............... 101.58333

Actual Vol. Flow Rate (acfm):.................. 207604
Dry Standard Plow Rate (dscfm) :........... 176690

Standard Flow Rate (scfm): .•••..•••..•.••••.•••• 192830



# 86Date: Project: customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV030 PITOT TRAVERSE DATA

Traverse Nwnber: Condition: Time: Data Taken By: 3 >90%

Start- 9:45 TW/RB End- 9:56

Pressure, Barornetric(Hg"): Pressure, Static (H20") : Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 19.0 80.5 0.085 27.914

Moisture Determination Initial Volume ••••......... 245.165 Final Volume ....•••••.••.•. 269.588 Meter Temperature••••..•... 90.0 Meter Delta H 

## ........... 2.0 Meter Volume dscf. ••••.•.•. 23.427

Traverse Delta SQRT Temp. Point: (Ap) (Ap) (oF) A-l 0.71 0.8426 104 2 0.77 0.8775 104 3 0.90 0.9487 105 4 0.92 0.9592 105 5 0.98 0.9899 105 6 0.95 0.9747 105 7 0.94 0.9695 105 8 0.95 0.9747 105 9 0.93 0.9644 105 10 0.94 0.9695 105 11 0.89 0.9434 104 12 0.85 0.9220 97 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration•..•••••• 1. 005 Imp. # Tare Final Net

1 719.8 753.6 33.8 2 754.0 759.6 5.6 3 517.5 518.7 1.2 4 772.9 778.7 5.8 TOTAL 46.4

Traverse Delta SQRT Temp. Point: (Ap) (Ap) B-1 0.83 0.911 102 2 0.85 0.922 103 3 0.88 0.938 103 4 0.94 0.970 103 5 0.98 0.990 103 6 0.96 0.980 103 7 0.95 0.975 104 8 0.94 0.970 103 9 0.95 0.975 103 10 0.90 0.949 104 11 0.88 0.938 103 12 0.85 0.922 93

Average Delta (Ap): 0.9017
Average SQRT Delta (Ap) : ...•.•.•. 0.9489

Flue Gas Veloc1ty,ft/sec: •••..... 56.297 Average Flue Temperature (Ts):............... 103.16667

Actual Vol. Flow Rate (acfm):.................. 201264
Dry Standard Flow Rate (dscfm) :........... 170494

Standard Flow Rate (scfm): •••......•••••.•.•...• 186415



# 87Customer: Location: Source: Hibbing Taconite Hibbing, MN SV031 Test Date: Job Number: Box Truck: Operator: 5/07-5/08/07 M22A0346 E11 MBA
NO. Calibration/Bias Calculations Project: M22A0346

Date: 5/07·5/08/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 0.6 0.6 0.1 Pass Mid gas 218.1 217.0 1.1 0.3 Pass High gas 413.0 417.4 4.4 1.1 Pass

### ~span Value: Start End Time Time Run Cma Precal Bias Posteal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 17:00 18:00 1 ",218;1' 217.0 P 1,',','217.0 P P , 0.0'
" P ", 

## . 0.6•.. P P , ,'69:3 69.4 0.3 217.0 6:11 7:11 2 218.1 217.0 P 217.0 P P 0.6 P '0:6'" P P ,66.6 68.5 0.6 217.0 7:38 8:38 3 218.1 217.0 P 217.0 ' P P 0.6 P 

### '" '0.6 P P 68.7 68.6 0.6 217.0

Notes Cma = Concentration of Cal Gas C = Average value of test Cgas = Corrected gas value of test Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 88

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run

### # System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### 0.00 -0.14 0.60 0.00 0.14 Upscale Gas 

### 217.00 0.00 216.98 0.00 0.00 2 Zero Gas 

### 0.60 0.00 0.60 0.00 0.00 Upscale Gas 

### 216.98 0.00 217.00 0.00 0.00 3 Zero Gas 

### 0.60 0.00 0.60 0.00 0.00 Upscale Gas 

### 217.00 0.00 217.00 0.00 0.00



# 89Date: Project: customer: Location: Source: 5/7/2007 M22A0346 Hibbing Taconite Hibbing, MN SV031 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken 5y: 1 >90%

Start- 17:03 TW/RB End- 17: 13

Pressure. 5arometric(HgU): Pressure. Static(H20U): Pressure. Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (5ws): Molecular Wt. of Gas. Wet: 0.5 20.0 79.5 0.065 28.17 Rectangular Duct: Flue Area: inches by inches 59.583 sq. feet

Moisture Determination Initial Volume ••.••..•.•..• Final Volume ...•...•.•••.•• Meter Temperature .••.•..... Meter Delta H ••.......•. Meter Volume dscf..•.•.•.•.

Traverse Delta SQRT Point: (liP) (liP) A-l 0.63 0.7937 2 0.71 0.8426 3 0.74 0.8602 4 0.81 0.9000 5 0.85 0.9220 6 0.91 0.9539 7 0.96 0.9798 8 0.91 0.9539 9 0.89 0.9434 10 0.88 0.9381 11 0.79 0.8888 12 0.75 0.8660 283.476 307.172 77.0 2.0 23.280
Temp. (OF) 115 115 115 i115 115 115 115 115 115 115 115 110 Meter Calibration•.....•.• 1.005 Imp. # Tare Final Net

1 789.4 814.9 25.5 2 767.3 770.4 3.1 3 711. 9 712.2 0.3 4 803.6 809.1 5.5 TOTAL 34.4

Traverse Delta SQRT Temp. Point: (lip) (liP) 5-1 0.73 0.854 115 2 0.83 0.911 115 3 0.90 0.949 115 4 0.93 0.964 115 5 0.96 0.980 115 6 0.98 0.990 115 7 0.91 0.954 115 8 0.93 0.964 115 9 0.88 0.938 115 10 0.78 0.883 115 11 0.75 0.866 115 12 0.63 0.794 109

Average Delta (lip): •.•....••••••. 0.8350
Average SQRT Delta (lip) : .....•••. 0.9121

Flue Gas Velocity,ft/sec: •....•.. 54.406 Average Flue Temperature (Ts):............... 114.54167

Actual Vol. Flow Rate (acfm):.................. 194503
Dry Standard Flow Rate (dscfm) :........... 165083

Standard Flow Rate {scfm): .....•••••••••..••..•• 176584



# 90Date: Project: Customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV031 PITOT TRAVERSE DATA

Traverse NWllber: Condition: Time: Data Taken By: 2 >90%

Start- 7: 00 TW/RB End- 7: 11

pressure, Barometric (Hg") : Pressure, Static (H20") : Pressure, Stack(Hg"): Pitot Tube Coefficient(Cp): Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(\): Oxygen Content(\): Nitrogen Content(\): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 19.0 80.5 0.064 28.148 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Moisture Determination Initial Volume .•••••••••.•• 257.123 Final Volume •••.••..•.••.•• 281. 396 Meter Temperature ••........ 72.0 Meter Delta H 

### ........... 2.0 Meter Volume dscf.••.•.••.• 24.071

Traverse Delta SQRT Temp. Point: (tiP) (tip) (oF) A-l 0.75 0.8660 112 2 0.85 0.9220 112 3 0.90 0.9487 113 4 0.97 0.9849 113 5 1.10 1. 0488 114 6 1.10 1. 0488 114 7 1. 00 1. 0000 114 8 0.94 0.9695 114 9 0.91 0.9539 114 10 0.86 0.9274 114 11 0.82 0.9055 114 12 0.73 0.8544 86

Average Delta (tiP): 0.8879
Average SQRT Delta (tiP): .••.•.•.. 0.9404

Flue Gas Velocity,ft/sec: •..•..•. 55.943 Meter Calibration•.•.•.•.• 1. 005 Imp. # Tare Final Net

1 794.3 821.1 26.8 2 736.5 738.9 2.4 3 741.2 742.0 0.8 4 803.3 808.1 4.8 TOTAL 34.8

Traverse Delta SQRT Temp. Point: (tip) (tip) B-1 0.68 0.825 113 2 0.71 0.843 114 3 0.78 0.883 113 4 0.84 0.917 114 5 0.95 0.975 114 6 0.98 0.990 114 7 1. 00 1. 000 114 8 1.00 1. 000 114 9 0.90 0.949 114 10 0.92 0.959 114 11 0.85 0.922 114 12 0.77 0.877 78

Average Flue Temperature (Ts):............... 111

Actual Vol. Flow Rate (acfm):.................. 199996
Dry Standard Flow Rate (dscfm) :........... 171040

Standard Flow Rate (scfm): •..••...•.••.••••.••.. 182699



# 91.Date: Project: Customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV03l PITOT TRAVERSE DATA

Traverse Nwnber: Condition: Time: Data Taken By: >90% Start- 8:10 TW/RB End- 8:20

Pressure, Barometric (Hgn) : Pressure, Static (H20n) : Pressure, Stack(Hgn): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 29.60 31. 78 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 19.0 80.5 0.082 27.955

Moisture Determination Initial Volume .......•.•.•. 195.719 Final Volume •.•••••••.•••.. 219.929 Meter Temperature ••.•...... 80.0 Meter Delta H 0.0 aa 0 ••••• 2.0 Meter Volume dscf. •.•.•••.. 23.653

Traverse Delta SQRT Temp. Point: (Ap) (Ap) (oF) A-I 0.74 0.8602 115 2 0.82 0.9055 115 3 0.91 0.9539 115 4 0.94 0.9695 115 5 0.97 0.9849 115 6 0.98 0.9899 115 7 0.90 0.9487 115 8 0.95 0.9747 115 9 0.85 0.9220 115 10 0.77 0.8775 115 11 0.73 0.8544 115 12 0 ..61 0.7810 113 Rectangular Duct: Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration ...•..... 1.005 Imp. # Tare Final Net

1 734.7 770.1 35.4 2 698.3 700.8 2.5 3 619.4 621.2 1.8 4 637.6· 642.5 4.9 TOTAL 44.6

Traverse Delta SQRT Temp. Point: (Ap) (Ap) B-1 0.65 0.806 112 2 0.72 0.849 112 3 0.74 0.860 112 4 0.80 0.894 112 5 0.84 0.917 112 6 0.90 0.949 112 0.93 0.964 112 8 0.94 0.970 112 9 0.90 0.949 112 10 0.89 0.943 112 11 0.80 0.894 112 12 0.77 0.877 106

Average Delta (Ap): •••••••••••••• 0.8354
Average SQRT Delta (Ap): ••••••••• 0.9123

Flue Gas Velocity,ft/sec: .•.....• 52.607 Average Flue Temperature (Ts):............... 113.16667

Actual Vol. Flow Rate (acfm):.................. 188072
Dry Standard Flow Rate (dscfm) :........... 169084

Standard Flow Rate (scfm): •.•.••.....•••••.•.... 184116



# 92Customer: Location: Source: Hibbing Taconite Hibbing, MN SV032 Test Date: Job Number: Box Truck: Operator: 5/07- 05/08/07 M22A0346 E11 MBA 

### NO. Calibration/Bias Calculations Project: M22A0346

Date: 5/07- 05/08/07
Analyzer Calibration Responses Cylinder Analyzer Absolute Difference Value Response Difference (ppm) (ppm) (ppm) (% of span) Status Zero gas 0.0 0.7 0.7 0.2 Pass Mid gas 218.1 215.6 2.5 0.6 Pass High gas 413.0 412.6 0.4 0.1 Pass

413 Ispan Value: Start End Time Time Run Cma Preeal Bias Posteal Bias Drift Pre zero Bias Post zero Bias Drift C Cgas Co Cm 14:22 15:22 1 218.1 212.2 P 212.7 .'. P P 1.1 

### .... P 

### 1/ 1:7 P P 99.1 100.9 1.4 212.5 15:39 16:39 2 218.1 212.7 P

.**218~7** . P P 1.7 P 0.7 P P ,96.8 •. 97.2 1.2 215.7 5:55 6:55 3 218.1 217.4 P 

## .. 217.7 P P 1.7 P 0.7.··. P P ·A03.1 102.7 1.2 217.6

Notes Cma = Concentration of Cal Gas C = Average value ottest Cgas = Corrected gas value ottest Co=Average Pre and Post Zero Cm=Average Pre and Post Span



# 93

### NOx Calibration Bias and Drift Summary

Initial Values Final Values Drift Run# System System System System (% of span) Calibration cal. Bias Calibration cal. Bias Response (% of span) Response (% of span) 

### 1 Zero Gas 

### 1.08 0.10 1.67 0.24 0.14 Upscale Gas 

### 212.20 -0.81 212.70 -0.69 0.12 2 Zero Gas 

### 1.67 0.24 0.66 0.00 -0.24 Upscale Gas 

### 212.70 -0.69 218.70 0.76 1.45 3 Zero Gas 

### 1.66 0.24 0.66 0.00 -0.24 Upscale Gas 

### 217.43 0.45 217.73 0.53 0.07



# 94PITOT TRAVERSE DATA

Date: 5/7/2007 Traverse Number: 1 Project: M22A0346 Condition: >90% Customer: Hibbing Taconite Time: Start- 14:41 End- 14: 59 Location: Hibbing, MN Data Taken By: TW/RB Source: SV032

Pressure, Barometric (Hg") : Pressure, Static(H20"): Pressure, Stack(Hg"): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(\): Oxygen Content(\): Nitrogen Content(\): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.6 19.0 80.4 0.058 28.22 Rectangular Duct: Flue Area:

Moisture Determination Initial Volume ..•.......... Final Volume

.. Meter Temperature

. Meter Delta H •..••.••.•• Meter Volume dscf.••......•

Traverse Delta SQRT Point:**(~p)** (M) A-1 0.62 0.7874 2 0.75 0.8660 3 0.87 0.9327 4 0.98 0.9899 5 1.10 1. 0488 6 1.10 1. 0488 7 1.10 1.0488 8 0.99 0.9950 9 1. 00 1.0000 10 0.91 0.9539 11 0.79 0.8888 12 0.66 0.8124 inches by 59.583

84.338 108.025 77.0 2.0 23.271
Temp. (oF) 124 124 124 124. 124 124 124 124 124 124 124 117 inches sq. feet

Meter Calibration•••.•.••• 1.005 Imp. # Tare Final Net

1 771.6 794.9 23.3 2 729.2 731. 0 1.8 3 520.0 519.9 -0.1 4 807.3 812.9 5.6 TOTAL 30.6

Traverse Delta SQRT Temp. Point:**(~P) (~P)**  B-1 0.69 0.831 124 2 0.81 0.700 124 3 0.95 0.975 124 4 0.98 0.990 124 5 1.10 1.049 124 6 1.20 1.095 124 7 0.98 0.990 124 8 0.96 0.980 124 9 0.88 0.938 124 10 0.89 0.943 124 11 0.76 0.872 122 12 0.60 0.775 116

Average Delta**(~P):** •..••.......•. 0.9029 Average Flue Temperature (Ts): •••••.•..•...•. 123.29167
Average SQRT Delta**(~P)** : 0.9379 Actual Vol. Flow Rate (acfm):.................. 201346

Flue Gas Velocity,ft/sec: •.•.•... 56.320 Dry Standard Flow Rate (dscfm) : ...•..•.••• 169542

Standard Flow Rate (scfm): •.••..•..••.••••••.••• 180054



# 95Date: Project: Customer: Location: Source: 5/7/2007 M22A0346 Hibbing Taconite Hibbing, MN SV032 PITOT TRAVERSE DATA

Traverse Nwnber: Condition: Time: Data Taken By: 2 >90%

Start- 15:52 TW/RB End- 16: 01

Pressure, Barometric (Hgn) : Pressure, Static (H20n) : Pressure, Stack(Hgn): Pitot Tube Coefficient (Cp) : Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 19.0 80.5 0.060 28.188 Rectangular Duct: Flue Area: 0.00 inches by 0.00 inches 59.583 sq. feet

Moisture Determination Initial Volume .••.•..••••.• 108.212 Final Volume .••............ 131. 450 Meter Temperature .......... 75.0 Meter Delta H 

### ........... 2.0 Meter Volume dscf•.••.••.•. 22.915

Traverse Delta SORT Temp. Point: (!>P) (!>p) (OF) A-l 0.59 0.7681 122 2 0.82 0.9055 122 3 0.89 0.9434 123 4 0.95 0.9747 123 5 1. 00 1. 0000 123 6 1. 20 1. 0954 123 7 0.99 0.9950 123 8 1.10 1.0488 123 9 0.97 0.9849 123 10 0.96 0.9798 123 11 0.81 0.9000 123 12 0.62 0.7874 117

Average Delta (!>P): 0.8963
Average SORT Delta (!>P) : •••.....• 0.9426

Flue Gas Veloc1ty,ft/sec: .•.•.•.. 56.606 Meter Calibration .•..••... 1. 005 Imp. # Tare Final Net

1 789.3 807.9 18.6 2 699.2 705.3 6.1 3 737.7 737.9 0.2 4 814.1 820.3 6.2 TOTAL 31.1

Traverse Delta SORT Temp. Point: (!>P) (!>P) B-1 0.67 0.819 123 2 0.79 0.889 123 3 0.89 0.943 123 4 0.97 0.985 123 5 1.10 1.049 123 6 1.10 1.049 123 7 0.97 0.985 132 8 0.97 0.985 123 9 0.93 0.964 123 10 0.87 0.933 123 11 0.76 0.872 121 12 0.59 0.768 115

Average Flue Temperature (Ts):............... 122.625

Actual Vol. Flow Rate (acfm):.................. 202366
Dry Standard Flow Rate (dscfm) :........... 170277

Standard Flow Rate (scfm): 181173



# 96Date: Project: Customer: Location: Source: 5/8/2007 M22A0346 Hibbing Taconite Hibbing, MN SV032 PITOT TRAVERSE DATA

Traverse Number: Condition: Time: Data Taken By: 3 >90%

Start- 6:26 TW/RB End- 6:35

Pressure, Barometric (Hg") : Pressure, Static(H20"): Pressure, Stack(Hg"): Pitot Tube Coefficient(Cp): Duct Diameter (in): 29.60 -0.80 29.54 0.840 104.52 Carbon Dioxide Content(%): Oxygen Content(%): Nitrogen Content(%): Water Vapor in Flue Gas (Bws): Molecular Wt. of Gas, Wet: 0.5 19.0 80.5 0.083 27.942

Moisture Determination Initial Volume ...•.•••••••• 171.352 Final Volume .•••.•.•.....•• 195.462 Meter Temperature ..•••••••• 85.0 Meter Delta H 

### ........... 2.0 Meter Volume dscf ......•.•• 23.339

Traverse Delta SORT Temp. Point: (Ap) (Ap) (oF) A-1 0.62 0.7874 121 2 0.77 0.8775 121 3 1. 00 1. 0000 121 4 1.10 1.0488 121 5 1.20 1.0954 121 6 1.10 1. 0488 121 7 1.10 1.0488 120 8 1. 00 1. 0000 120 9 0.96 0.9798 120 10 0.91 0.9539 120 11 0.56 0.7483 120 12 0.72 0.8485 111 Rectangular Duct, Flue Area: 0.00 inches by 59.583 0.00 inches sq. feet

Meter Calibration .•.•••••• 1.005 Imp. # Tare Final Net

1 815.3 851. 0 35.7 2 751. 0 754.0 3.0 3 517.0 517.5 0.5 4 767.4 772.9 5.5 TOTAL 44.7

Traverse Delta SORT Temp. Point: (AP) (Ap) B-1 0.80 0.894 121 2 0;89 0.943 121 3 1.10 1. 049 121 4 1.10 1.049 121 5 0.13 0.361 121 6 1.10 1.049 121 7 1.10 1. 049 121 8 0.99 0.995 121 9 0.95 0.975 120 10 0.83 0.911 120 11 0.77 0.877 120 12 0.65 0.806 109

Average Delta (Ap): ..•••••....•.• 0.8938
Average SORT Delta (Ap) : •.••...•• 0.9331

Flue Gas Ve1oc1ty,ft/sec: ••••••.. 56.143 Average Flue Temperature (Ts):............... 119.75

Actual Vol. Flow Rate (acfm):.................. 200712
Dry Standard Flow Rate (dscfm) :........... 165626

Standard Flow Rate \scfm): •.•••••...•..••••••.•. 180583



# 97SV021 SV021 SV021 Run 1 Run 2 Run 3 Date: 5/1/07 Date: 5/1/07 Date: 5/1/07 NOX NOX NOX Time PPM Time PPM Time PPM



### ----------------- ----------------- --------------- 6:38 37.4 7:50 30.4 9:00 33.2 6:39 35.0 7:51 29.9 9:01 32.9 6:40 36.9 7:52 29.4 9:02 33.0 6:41 36.3 7:53 30.2 9:03 32.4 6:42 35.5 7:54 30.6 9:04 32.5 6:43 34.4 7:55 30.2 9:05 31.9 6:44 34.9 7:56 29.1 9:06 31.5 6:45 33.1 7:57 28.9 9:07 33.4 6:46 35.5 7:58 29.3 9:08 35.6 6:47 34.3 7:59 30.2 9:09 35.3 6:48 34.1 8:00 29.9 9:10 34.3 6:49 33.8 8:01 30.3 9:11 33.2 6:50 33.5 8:02 31.2 9:12 32.8 6:51 32.1 8:03 31.2 9:13 33.1 6:52 32.2 8:04 31.5 9:14 33.7 6:53 33.1 8:05 32.4 9:15 32.7 6:54 34.4 8:06 32.3 9:16 31.3 6:55 35.2 8:07 33.2 9:17 31.1 6:56 34.8 8:08 31.4 9:18 30.9 6:57 34.0 8:09 32.0 9:19 37.3 6:58 32.2 8:10 35.0 9:20 38.7 6:59 34.2 8:11 33.3 9:21 36.4 7:00 35.2 8:12 32.4 9:22 35.4 7:01 33.2 8:13 32.9 9:23 35.2 7:02 33.0 8:14 33.2 9:24 36.6 7:03 34.3 8:15 34.2 9:25 37.3 7:04 34.2 8:16 34.6 9:26 37.9 7:05 33.8 8:17 32.9 9:27 37.1 7:06 33.9 8:18 32.4 9:28 37.2 7:07 33.1 8:19 33.9 9:29 36.8 7:08 33.5 8:20 33.4 9:30 36.9 7:09 34.6 8:21 31.6 9:31 36.3 7:10 33.7 8:22 33.0 9:32 35.4 7:11 33.7 8:23 33.1 9:33 36.1 7:12 34.2 8:24 33.2 9:34 36.6 7:13 34.8 8:25 34.2 9:35 37.2 7:14 33.1 8:26 32.9 9:36 37.5 7:15 32.7 8:27 31.2 9:37 39.0 7:16 32.8 8:28 33.0 9:38 37.1 7:17 31.5 8:29 33.4 9:39 43.2 7:18 33.2 8:30 33.1 9:40 41.7 7:19 32.5 8:31 34.2 9:41 42.0 7:20 32.7 8:32 33.0 9:42 41.6 7:21 32.2 8:33 34.0 9:43 41.2 7:22 32.9 8:34 33.4 9:44 40.3 7:23 32.7 8:35 33.1 9:45 39.9 7:24 31.8 8:36 34.2 9:46 40.4 7:25 33.4 8:37 34.4 9:47 39.5 7:26 32.3 8:38 33.2 9:48 40.6 7:27 33.9 8:39 33.2 9:49 40.3 7:28 35.3 8:40 33.7 9:50 40.8 7:29 34.1 8:41 33.9 9:51 42.6 7:30 34.2 8:42 33.2 9:52 41.7 7:31 33.1 8:43 32.9 9:53 39.5 7:32 32.2 8:44 33.7 9:54 40.9 7:33 33.3 8:45 33.0 9:55 40.0 7:34 33.9 8:46 31.9 9:56 39.7 7:35 33.6 8:47 31.9 9:57 41.0 7:36 33.5 8:48 32.4 9:58 38.8 7:37 33.2 8:49 33.2 9:59 39.4



### ----------------- ----------------- -------------_. MAX : 37.4 MAX : 35.0 MAX : 43.2 MIN: 31.5 MIN : 28.9 MIN : 30.9 AVG: 33.8 AVG: 32.4 AVG: 37.0 SCANS: 60 SCANS: 60 SCANS: 60 

# 98SV022 SV022 SV022 Run 1 Run 2 Run 3 Date: 5/1/07 Date: 5/1/07 Date: 5/1/07 NOX NOX NOX Time PPM Time PPM Time PPM

-._..---.----_.-. ----------------- --------------_. 6:31 63.2 7:50 53.7 9:05 58.3 6:32 57.9 7:51 52.9 9:06 58.1 6:33 57.5 7:52 54.2 9:07 61.3 6:34 57.3 7:53 55.5 9:08 65.1 6:35 56.1 7:54 56.8 9:09 64.7 6:36 56.6 7:55 55.9 9:10 62.2 6:37 58.7 7:56 53.9 9:11 60.8 6:38 57.4 7:57 53.9 9:12 60.7 6:39 56.2 7:58 55.4 9:13 59.8 6:40 58.8 7:59 54.9 9:14 61.8 6:41 58.7 8:00 53.6 9:15 59.3 6:42 58.3 8:01 55.2 9:16 60.9 6:43 56.0 8:02 56.2 9:17 66.1 6:44 56.1 8:03 56.6 9:18 67.7 6:45 53.8 8:04 56.9 9:19 68.5 6:46 56.5 8:05 56.9 9:20 68.7 6:47 56.2 8:06 56.7 9:21 67.5 6:48 56.1 8:07 58.1 9:22 63.8 6:49 56.3 8:08 53.6 9:23 64.7 6:50 56.0 8:09 55.4 9:24 66.0 6:51 53.7 8:10 60.1 9:25 67.7 6:52 53.7 8:11 58.6 9:26 69.0 6:53 55.8 8:12 56.1 9:27 66.6 6:54 58.4 8:13 57.1 9:28 68.0 6:55 59.4 8:14 57.2 9:29 66.4 6:56 59.7 8:15 59.3 9:30 66.7 6:57 57.9 8:16 60.0 9:31 66.2 6:58 55.2 8:17 57.0 9:32 64.6 6:59 58.0 8:18 56.6 9:33 66.1 7:00 60.2 8:19 58.4 9:34 66.7 7:01 56.3 8:20 57.0 9:35 66.7 7:02 55.8 8:21 54.0 9:36 68.3 7:03 58.7 8:22 57.0 9:37 67.3 7:04 58.4 8:23 57.4 9:38 67.1 7:05 57.4 8:24 57.8 9:39 69.1 7:06 57.8 8:25 58.7 9:40 67.1 7:07 57.1 8:26 57.5 9:41 68.6 7:08 58.0 8:27 54.1 9:42 67.7 7:09 60.6 8:28 56.9 9:43 67.2 7:10 58.7 8:29 57.1 9:44 65.3 7:11 58.7 8:30 56.6 9:45 63.6 7:12 58.3 8:31 58.0 9:46 65.0 7:13 60.6 8:32 56.7 9:47 65.3 7:14 57.2 8:33 57.4 9:48 65.3 7:15 56.2 8:34 56.7 9:49 65.5 7:16 56.5 8:35 56.1 9:50 66.2 7:17 54.4 8:36 58.3 9:51 67.1 7:18 57.8 8:37 59.2 9:52 68.2 7:19 57.1 8:38 56.9 9:53 64.1 7:20 56.2 8:39 57.3 9:54 64.6 7:21 56.4 8:40 58.5 9:55 64.9 7:22 57.3 8:41 58.8 9:56 63.6 7:23 56.1 8:42 58.5 9:57 66.9 7:24 54.7 8:43 56.7 9:58 63.7 7:25 57.4 8:44 57.7 9:59 63.8 7:26 55.9 8:45 57.5 10:00 64.8 7:27 57.3 8:46 56.4 10:01 63.9 7:28 60.3 8:47 55.5 10:02 62.2 7:29 59.2 8:48 56.3 10:03 64.6 7:30 58.2 8:49 57.2 10:04 63.1

----------------- ----------------- 

### --------------- MAX : 63.2 MAX : 60.1 MAX : 69.1 MIN: 53.7 MIN : 52.9 MIN: 58.1 AVO: 57.3 AVO: 56.7 AVO: 65.1 SCANS: 60 SCANS: 60 SCANS: 60



# 99SV023 SV023 SV023 Run 1 Run 2 Run 3 Date: 5/1/07 Date: 5/1/07 Date: 5/1/07 NOX NOX NOX Time PPM Time PPM Time PPM

----------------- 

### ----------------- --------.---_. 10:25 87.6 11:43 95.7 12:58 92.0 10:26 87.8 11:44 94.0 12:59 91.9 10:27 89.5 11:45 94.7 13:00 96.2 10:28 94.3 11:46 98.9 13:01 93.7 10:29 91.4 11:47 99.5 13:02 89.8 10:30 90.5 11:48 98.8 13:03 92.0 10:31 93.8 11:49 94.8 13:04 95.7 10:32 89.9 11:50 96.8 13:05 96.0 10:33 89.8 11:51 94.0 13:06 92.6 10:34 90.9 11:52 97.3 13:07 94.3 10:35 91.9 11:53 93.6 13:08 96.3 10:36 91.3 11:54 92.6 13:09 94.8 10:37 92.8 11:55 93.1 13:10 94.0 10:38 91.8 11:56 92.5 13:11 91.4 10:39 92.5 11:57 93.4 13:12 92.2 10:40 94.1 11:58 95.1 13:13 91.0 10:41 96.6 11:59 96.2 13:14 91.2 10:42 95.9 12:00 98.0 13:15 92.1 10:43 93.7 12:01 95.4 13:16 90.3 10:44 90.7 12:02 94.4 13:17 93.9 10:45 91.2 12:03 98.5 13:18 94.7 10:46 90.3 12:04 96.2 13:19 94.2 10:47 90.4 12:05 93.3 13:20 91.5 10:48 90.7 12:06 94.8 13:21 91.4 10:49 90.6 12:07 94.2 13:22 87.4 10:50 87.7 12:08 97.5 13:23 89.8 10:51 86.6 12:09 98.5 13:24 91.3 10:52 90.9 12:10 98.9 13:25 89.5 10:53 90.4 12:11 98.6 13:26 91.2 10:54 90.7 12:12 98.6 13:27 94.6 10:55 90.4 12:13 93.7 13:28 90.3 10:56 91.3 12:14 93.3 13:29 89.9 10:57 93.6 12:15 93.7 13:30 89.0 10:58 92.1 12:16 96.9 13:31 89.0 10:59 89.5 12:17 97.4 13:32 92.4 11:00 91.0 12:18 97.2 13:33 94.4 11:01 93.3 12:19 97.5 13:34 94.7 11:02 93.2 12:20 100.8 13:35 94.6 11:03 94.1 12:21 99.1 13:36 92.9 11:04 93.3 12:22 94.6 13:37 97.7 11:05 94.2 12:23 93.1 13:38 96.0 11:06 95.0 12:24 95.3 13:39 93.6 11:07 94.5 12:25 94.1 13:40 91.3 11:08 92.3 12:26 96.0 13:41 92.2 11:09 92.5 12:27 97.5 13:42 89.1 11:10 91.6 12:28 96.3 13:43 88.6 11:11 91.8 12:29 96.0 13:44 94.8 11:12 89.8 12:30 94.6 13:45 95.6 11:13 89.8 12:31 94.1 13:46 95.2 11:14 90.5 12:32 95.1 13:47 93.7 11:15 91.6 12:33 93.7 13:48 93.9 11:16 91.6 12:34 96.1 13:49 92.7 11:17 90.8 12:35 96.6 13:50 95.0 11:18 88.6 12:36 93.9 13:51 93.6 11:19 91.0 12:37 93.8 13:52 91.7 11:20 94.0 12:38 92.3 13:53 89.5 11:21 92.5 12:39 96.7 13:54 88.7 11:22 90.3 12:40 96.8 13:55 93.1 11:23 91.1 12:41 94.4 13:56 91.1 11:24 92.0 12:42 96.2 10:04 93.1



### ----------------- ----------------- -------------_. MAX : 96.6 MAX : 100.8 MAX : 97.7 MIN: 86.6 MIN : 92.3 MIN: 87.4 AVG: 91.6 AVG: 95.7 AVG: 92.6 SCANS: 60 SCANS: 60 SCANS: 60SV024 SV024 SV024 Run 1 Run 2 Run 3 Date: 5/1/07 Date: 5/2/07 Date: 5/2/07 NOX NOX NOX Time PPM Time PPM Time PPM**~----------------** 

### ----------------- ----------.---- 14:13 103.0 5:46 95.9 7:00 91.1 14:14 100.2 5:47 97.7 7:01 92.7 14:15 103.5 5:48 94.5 7:02 93.1 14:16 104.0 5:49 93.1 7:03 92.3 14:17 100.2 5:50 92.9 7:04 95.2 14:18 97.4 5:51 93.9 7:05 94.8 14:19 97.8 5:52 96.7 7:06 96.5 14:20 102.5 5:53 97.1 7:07 89.7 14:21 102.8 5:54 97.8 7:08 90.6 14:22 106.0 5:55 97.3 7:09 90.5 14:23 104.0 5:56 98.2 7:10 88.9 14:24 104.2 5:57 96.7 7:11 85.1 14:25 104.0 5:58 97.5 7:12 89.3 14:26 105.8 5:59 97.5 7:13 99.8 14:27 105.8 6:00 98.2 7:14 103.0 14:28 105.6 6:01 97.4 7:15 102.6 14:29 105.1 6:02 100.5 7:16 98.8 14:30 109.7 6:03 100.0 7:17 96.8 14:31 108.7 6:04 96.1 7:18 98.6 14:32 105.4 6:05 96.9 7:19 100.8 14:33 104.5 6:06 98.5 7:20 105.8 14:34 109.1 6:07 101.2 7:21 105.3 14:35 109.3 6:08 100.7 7:22 103.6 14:36 106.0 6:09 97.5 7:23 101.5 14:37 104.3 6:10 97.8 7:24 100.6 14:38 108.7 6:11 97.7 7:25 100.3 14:39 108.0 6:12 100.7 7:26 99.0 14:40 110.3 6:13 97.6 7:27 100.5 14:41 109.5 6:14 92.6 7:28 101.1 14:42 105.0 6:15 94.1 7:29 102.3 14:43 101.8 6:16 94.7 7:30 100.5 14:44 105.7 6:17 96.3 7:31 98.7 14:45 104.0 6:18 98.8 7:32 101.7 14:46 101.2 6:19 98.5 7:33 97.8 14:47 102.7 6:20 103.7 7:34 97.3 14:48 107.7 6:21 102.0 7:35 94.0 14:49 102.0 6:22 94.2 7:36 94.9 14:50 104.0 6:23 99.5 7:37 98.5 14:51 105.7 6:24 101.8 7:38 98.5 14:52 100.8 6:25 101.2 7:39 94.9 14:53 101.2 6:26 100.4 7:40 96.0 14:54 102.8 6:27 97.2 7:41 99.7 14:55 99.5 6:28 97.6 7:42 101.9 14:56 100.6 6:29 100.2 7:43 99.9 14:57 103.1 6:30 96.1 7:44 97.3 14:58 101.7 6:31 87.8 7:45 96.9 14:59 100.7 6:32 92.0 7:46 96.8 15:00 100.5 6:33 92.5 7:47 100.0 15:01 100.8 6:34 94.2 7:48 102.1 15:02 104.8 6:35 96.3 7:49 97.8 15:03 99.6 6:36 96.2 7:50 97.6 15:04 100.2 6:37 94.2 7:51 96.5 15:05 101.4 6:38 91.7 7:52 97.3 15:06 104.1 6:39 93.1 7:53 94.3 15:07 103.2 6:40 95.2 7:54 93.3 15:08 102.5 6:41 93.0 7:55 88.4 15:09 102.3 6:42 87.5 7:56 87.8 15:10 103.3 6:43 93.7 7:57 83.6 15:11 100.9 6:44 98.0 7:58 84.6 15:12 101.2 6:45 93.7 7:59 84.7



### ----------------- --------------- --------------- MAX : 110.3 MAX : 103.7 MAX : 105.8 MIN : 97.4 MIN : 87.5 MIN: 83.6 AVG: 103.7 AVG: 96.6 AVG: 96.4 SCANS: 60 SCANS: 60 SCANS: 60**~:~** 

# (?1 .iL -"'SV025 SV025 SV025 Run 1 Run 2 Run 3 Date: 5/2/07 Date: 5/2/07 Date: 5/2/07 NOX NOX NOX Time PPM Time PPM Time PPM

---------------- -------.--------- ---------------- 8'.37 99.5 10:42 107.3 11:57 96.0 8:38 101.9 10:43 109.3 11:58 110.0 8:39 102.2 10:44 110.0 11:59 109.9 8:40 104.0 10:45 108.8 12:00 110.8 8:41 105.1 10:46 104.3 12:01 104.8 8:42 105.9 10:47 102.3 12:02 114.6 8:43 104.3 10:48 107.0 12:03 118.0 8:44 106.2 10:49 107.0 12:04 113.4 8:45 104.8 10:50 110.2 12:05 114.5 8:46 105.7 10:51 110.6 12:06 116.6 8:47 104.2 10:52 107.1 12:07 116.7 8:48 101.2 10:53 106.0 12:08 114.1 8:49 99.2 10:54 108.0 12:09 112.5 8:50 103.6 10:55 110.8 12:10 112.6 8:51 102.6 10:56 108.3 12:11 114.9 8:52 101.6 10:57 112.2 12:12 120.3 8:53 99.7 10:58 112.3 12:13 124.0 8:54 98.4 10:59 108.8 12:14 119.7 8:55 97.5 11:00 110.6 12:15 115.0 8:56 95.8 11:01 107.8 12:16 115.3 8:57 94.8 11:02 107.7 12:17 116.1 8:58 97.8 11:03 106.7 12:18 120.2 8:59 99.7 11:04 106.5 12:19 119.3 9:00 98.1 11:05 107.6 12:20 117.7 9:01 96.0 11:06 106.5 12:21 118.1 9:02 97.7 11:07 107.5 12:22 115.5 9:03 99.7 11:08 107.3 12:23 116.1 9:04 100.9 11:09 104.0 12:24 118.3 9:05 100.6 11:10 103.8 12:25 117.0 9:06 97.6 11:11 106.3 12:26 113.3 9:07 100.1 11:12 105.1 12:27 111.5 9:08 97.6 11:13 108.3 12:28 111.5 9:09 101.0 11:14 110.1 12:29 109.9 9:10 105.1 11:15 107.9 12:30 115.7 9:11 102.7 11:16 105.0 12:31 118.2 9:12 106.9 11:17 102.8 12:32 114.8 9:13 104.5 11:18 105.8 12:33 113.2 9:14 100.0 11:19 103.7 12:34 109.1 9:15 99.9 11:20 95.8 12:35 108.2 9:16 100.5 11:21 102.2 12:36 104.4 9:17 101.7 11:22 101.2 12:37 108.6 9:18 104.2 11:23 102.9 12:38 113.5 9:19 107.9 11:24 104.9 12:39 109.7 9:20 110.0 11:25 105.7 12:40 115.5 9:21 111.7 11:26 109.4 12:41 113.7 9:22 108.6 11:27 108.2 12:42 110.1 9:23 105.0 11:28 108.0 12:43 108.4 9:24 103.5 11:29 107.6 12:44 109.8 9:25 100.9 11:30 105.4 12:45 104.9 9:26 104.4 11:31 106.8 12:46 106.4 9:27 105.9 11:32 106.0 12:47 110.0 9:28 106.4 11:33 111.0 12:48 113.2 9:29 107.2 11:34 115.1 12:49 113.3 9:30 107.3 11:35 113.5 12:50 113.0 9:31 106.7 11:36 113.1 12:51 112.3 9:32 110.7 11:37 108.4 12:52 116.0 9:33 106.4 11:38 109.5 12:53 113.4 9:34 105.3 11:39 107.8 12:54 111.8 9:35 103.0 11:40 111.9 12:55 107.1 9:36 101.9 11:41 114.4 12:56 115.1



### ----------------- ----------------- --------------_. MAX : 111.7 MAX : 115.1 MAX : 124.0 MIN: 94.8 MIN: 95.8 MIN : 96.0 AVG: 102.7 AVG: 107.5 AVG: 113.1 SCANS: 60 SCANS: 60 SCANS: 60SV026 SV026 SV026 Run 1 Run 2 Run 3 Date: 5/2/07 Date: 5/2/07 Date: 5/3/07 NOX NOX NOX Time PPM Time PPM Time PPM

--------------.- ._---------------- ------------- 13:11 106.8 14:32 108.8 5:45 101.9 13:12 104.9 14:33 106.4 5:46 104.8 13:13 102.8 14:34 110.2 5:47 103.5 13:14 105.3 14:35 105.3 5:48 102.6 13:15 106.0 14:36 103.1 5:49 100.6 13:16 105.6 14:37 103.3 5:50 100.9 13:17 108.0 14:38 108.4 5:51 99.5 13:18 103.2 14:39 105.5 5:52 101.2 13:19 102.2 14:40 108.1 5:53 103.6 13:20 103.9 14:41 106.7 5:54 103.5 13:21 104.2 14:42 106.7 5:55 102.4 13:22 104.1 14:43 107.1 5:56 99.8 13:23 100.7 14:44 103.1 5:57 98.6 13:24 97.9 14:45 100.1 5:58 99.0 13:25 104.0 14:46 104.5 5:59 98.2 13:26 106.6 14:47 104.8 6:00 100.7 13:27 105.6 14:48 107.0 6:01 103.5 13:28 101.3 14:49 102.2 6:02 103.7 13:29 102.7 14:50 104.3 6:03 100.7 13:30 105.0 14:51 105.9 6:04 101.1 13:31 101.6 14:52 104.9 6:05 99.2 13:32 98.6 14:53 99.9 6:06 103.1 13:33 99.0 14:54 104.0 6:07 101.3 13:34 101.3 14:55 109.4 6:08 96.9 13:35 100.2 14:56 104.5 6:09 98.3 13:36 104.3 14:57 100.8 6:10 100.0 13:37 105.4 14:58 101.2 6:11 99.3 13:38 103.7 14:59 106.6 6:12 96.0 13:39 100.2 15:00 108.7 6:13 94.4 13:40 96.2 15:01 106.6 6:14 99.9 13:41 95.7 15:02 102.8 6:15 99.4 13:42 98.1 15:03 103.8 6:16 97.9 13:43 101.8 15:04 102.8 6:17 99.0 13:44 106.4 15:05 103.8 6:18 96.8 13:45 108.5 15:06 104.4 6:19 97.4 13:46 107.8 15:07 102.1 6:20 100.9 13:47 105.7 15:08 102.3 6:21 99.4 13:48 103.8 15:09 102.4 6:22 103.4 13:49 99.7 15:10 102.3 6:23 104.9 13:50 105.0 15:11 102.1 6:24 103.3 13:51 107.2 15:12 95.5 6:25 101.5 13:52 110.9 15:13 95.9 6:26 98.9 13:53 108.3 15:14 102.0 6:27 96.4 13:54 106.4 15:15 104.9 6:28 97.9 13:55 108.7 15:16 106.6 6:29 101.6 13:56 109.7 15:17 106.0 6:30 101.3 13:57 109.2 15:18 107.5 6:31 94.7 13:58 107.0 15:19 110.5 6:32 96.3 13:59 111.5 15:20 108.1 6:33 95.8 14:00 109.3 15:21 107.5 6:34 97.3 14:01 105.8 15:22 106.8 6:35 81.3 14:02 104.2 15:23 108.2 6:36 83.2 14:03 104.5 15:24 108.7 6:37 92.9 14:04 105.5 15:25 109.8 6:38 91.4 14:05 108.5 15:26 109.2 6:39 93.8 14:06 106.2 15:27 105.5 6:40 98.4 14:07 104.2 15:28 103.1 6:41 94.1 14:08 103.2 15:29 101.5 6:42 96.4 14:09 103.5 15:30 104.3 6:43 98.9 14:10 100.2 15:31 107.2 6:44 99.6

----------------- 

### ---------------- --------------_. MAX : 111.5 MAX : 110.5 MAX : 104.9 MIN : 95.7 MIN: 95.5 MIN: 81.3 AVG: 104.3 AVG: 104.9 AVG: 98.9 SCANS: 60 SCANS: 60 SCANS: 60


# :103SV027 SV027 SV027 Run 1 Run 2 Run 3 Date: 5/1/07 Date: 5/1107 Date: 5/1/07 NOX NOX NOX Time PPM Time PPM Time PPM

---------------- ._---------------- --------------_. 7:01 69.6 8:13 66.1 9:33 66.1 7:02 69.2 8:14 67.5 9:34 66.5 7:03 66.2 8:15 67.9 9:35 69.6 7:04 67.1 8:16 69.1 9:36 71.2 7:05 65.2 8:17 69.3 9:37 71.4 7:06 64.3 8:18 65.7 9:38 69.2 7:07 65.0 8:19 64.4 9:39 67.9 7:08 63.3 8:20 65.8 9:40 67.1 7:09 65.7 8:21 66.6 9:41 67.5 7:10 65.5 8:22 67.1 9:42 66.7 7:11 65.8 8:23 69.4 9:43 68.8 7:12 65.4 8:24 69.9 9:44 65.9 7:13 63.3 8:25 69.6 9:45 66.2 7:14 66.3 8:26 67.2 9:46 67.3 7:15 67.0 8:27 67.3 9:47 64.1 7:16 67.7 8:28 65.0 9:48 63.4 7:17 64.3 8:29 64.7 9:49 60.9 7:18 66.8 8:30 67.6 9:50 62.6 7:19 69.4 8:31 70.0 9:51 65.6 7:20 71.1 8:32 71.5 9:52 62.4 7:21 68.1 8:33 70.7 9:53 66.4 7:22 66.6 8:34 68.5 9:54 65.6 7:23 65.1 8:35 67.1 9:55 67.9 7:24 66.7 8:36 65.2 9:56 68.2 7:25 70.8 8:37 62.1 9:57 65.9 7:26 70.3 8:38 65.3 9:58 66.1 7:27 69.0 8:39 65.7 9:59 66.8 7:28 69.4 8:40 65.6 10:00 68.6 7:29 70.5 8:41 63.3 10:01 68.3 7:30 70.8 8:42 66.9 10:02 69.3 7:31 67.4 8:43 66.1 10:03 70.6 7:32 67.6 8:44 67.7 10:04 69.4 7:33 68.5 8:45 63.8 10:05 69.9 7:34 69.7 8:46 66.5 10:06 68.6 7:35 71.7 8:47 67.0 10:07 67.6 7:36 70.6 8:48 68.3 10:08 63.6 7:37 69.6 8:49 67.8 10:09 62.8 7:38 68.2 8:50 67.0 10:10 66.8 7:39 68.9 8:51 65.3 10:11 69.3 7:40 67.2 8:52 64.7 10:12 69.4 7:41 66.8 8:53 64.9 10:13 69.4 7:42 64.3 8:54 66.4 10:14 68.0 7:43 65.3 8:55 64.4 10:15 65.4 7:44 63.3 8:56 63.5 10:16 67.4 7:45 68.9 8:57 65.1 10:17 67.3 7:46 68.1 8:58 69.1 10:18 69.4 7:47 67.9 8:59 68.8 10:19 68.9 7:48 65.7 9:00 67.4 10:20 68.4 7:49 64.4 9:01 69.7 10:21 66.0 7:50 65.3 9:02 67.8 10:22 67.2 7:51 67.1 9:03 66.3 10:23 65.9 7:52 65.8 9:04 68.1 10:24 67.9 7:53 65.5 9:05 66.5 10:25 66.8 7:54 67.5 9:06 67.1 10:26 68.5 7:55 70.5 9:07 64.0 10:27 64.4 7:56 68.2 9:08 66.2 10:28 64.7 7:57 69.7 9:09 69.4 10:29 68.6 7:58 69.6 9:10 68.8 10:30 66.7 7:59 71.1 9:11 71.3 10:31 70.6 8:00 70.6 9:12 68.4 10:32 70.5



### ----------------- ----------------- --------

______0 MAX : 71.7 MAX : 71.5 MAX : 71.4 MIN: 63.3 MIN: 62.1 MIN : 60.9 AVG: 67.5 AVG: 67.0 AVG: 67.2 SCANS: 60 SCANS: 60 SCANS: 60SV028 SV028 SV028 Run 1 Run 2 Run 3 Date: 5/3/07 Date: 5/3/07 Date: 5/3/07 NOX NOX NOX Time PPM Time PPM Time PPM**._.~----~---------** 

### ----------------- --------------- 10:54 51.0 12:10 52.8 13:26 53.4 10:55 50.9 12:11 52.7 13:27 53.5 10:56 50.9 12:12 51.2 13:28 53.1 10:57 49.2 12:13 51.9 13:29 53.6 10:58 49.5 12:14 52.3 13:30 52.1 10:59 49.0 12:15 51.5 13:31 53.6 11:00 48.8 12:16 51.7 13:32 53.3 11:01 51.8 12:17 52.8 13:33 53.9 11:02 54.1 12:18 53.6 13:34 52.8 11:03 54.6 12:19 51.5 13:35 52.4 11:04 54.3 12:20 52.7 13:36 52.1 11:05 53.6 12:21 52.1 13:37 52.0 11:06 53.9 12:22 52.9 13:38 53.0 11:07 52.3 12:23 52.7 13:39 54.3 11:08 52.8 12:24 51.4 13:40 53.4 11:09 53.0 12:25 52.9 13:41 51.4 11:10 51.3 12:26 53.1 13:42 53.7 11:11 52.7 12:27 51.2 13:43 53.9 11:12 54.0 12:28 49.5 13:44 52.3 11:13 52.0 12:29 50.5 13:45 56.3 11:14 53.6 12:30 51.3 13:46 56.3 11:15 52.4 12:31 50.6 13:47 55.1 11:16 51.2 12:32 49.0 13:48 52.4 11:17 51.6 12:33 50.5 13:49 51.6 11:18 53.3 12:34 53.6 13:50 50.2 11:19 54.2 12:35 52.4 13:51 52.8 11:20 54.4 12:36 54.9 13:52 52.6 11:21 51.5 12:37 54.6 13:53 50.2 11:22 51.0 12:38 54.3 13:54 49.8 11:23 49.3 12:39 52.6 13:55 51.5 11:24 52.1 12:40 52.9 13:56 51.2 11:25 50.9 12:41 54.8 13:57 53.6 11:26 51.5 12:42 54.5 13:58 52.3 11:27 50.3 12:43 55.4 13:59 50.9 11:28 48.8 12:44 55.3 14:00 50.7 11:29 48.9 12:45 53.4 14:01 48.7 11:30 50.2 12:46 52.9 14:02 49.8 11:31 52.7 12:47 53.3 14:03 51.0 11:32 51.9 12:48 53.1 14:04 53.1 11:33 53.0 12:49 51.6 14:05 52.3 11:34 50.5 12:50 51.1 14:06 52.0 11:35 48.8 12:51 52.3 14:07 53.8 11:36 50.9 12:52 50.1 14:08 52.2 11:37 52.2 12:53 49.8 14:09 53.4 11:38 53.2 12:54 53.3 14:10 54.7 11:39 54.8 12:55 52.9 14:11 56.2 11:40 56.1 12:56 51.2 14:12 56.6 11:41 55.5 12:57 53.2 14:13 56.5 11:42 53.2 12:58 51.5 14:14 55.3 11:43 54.0 12:59 51.9 14:15 56.2 11:44 51.1 13:00 52.9 14:16 55.6 11:45 52.7 13:01 50.1 14:17 54.8 11:46 53.6 13:02 51.6 14:18 55.0 11:47 52.5 13:03 51.5 14:19 53.8 11:48 52.4 13:04 51.3 14:20 53.3 11:49 51.9 13:05 51.0 14:21 52.1 11:50 51.3 13:06 50.8 14:22 51.8 11:51 51.3 13:07 52.1 14:23 51.0 11:52 50.9 13:08 50.9 14:24 52.9 11:53 52.4 13:09 53.4 14:25 52.7



### ----------------- ----------------- -------------- MAX : 56.1 MAX : 55.4 MAX : 56.6 MIN : 48.8 MIN : 49.0 MIN : 48.7 AVG: 52.0 AVG: 52.2 AVG: 53.0 SCANS: 60 SCANS: 60 SCANS: 60 

# 205SV029 SV029 SV029 Run 1 Run 2 Run 3 Date: 5/8/07 Date: 5/8/07 Date: 5/8/07 NOX NOX NOX Time PPM Time PPM Time PPM 

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

### ._-------------_. 10:52 34.1 12:02 33.5 13:12 32.9 10:53 34.8 12:03 32.8 13:13 32.4 10:54 34.6 12:04 32.7 13:14 32.9 10:55 35.2 12:05 32.5 13:15 31.5 10:56 35.7 12:06 32.0 13:16 31.8 10:57 35.0 12:07 32.5 13:17 33.0 10:58 35.0 12:08 32.2 13:18 32.3 10:59 33.4 12:09 33.5 13:19 31.8 11:00 34.3 12:10 33.5 13:20 32.0 11:01 33.4 12:11 32.7 13:21 32.2 11:02 35.0 12:12 32.0 13:22 32.5 11:03 34.3 12:13 31.9 13:23 33.2 11:04 33.9 12:14 32.0 13:24 32.4 11:05 33.5 12:15 32.7 13:25 32.0 11:06 34.3 12:16 33.5 13:26 32.1 11:07 34.8 12:17 33.8 13:27 32.4 11:08 35.2 12:18 33.3 13:28 32.9 11:09 34.8 12:19 33.3 13:29 32.8 11:10 33.8 12:20 32.8 13:30 32.6 11:11 35.0 12:21 32.9 13:31 31.8 11:12 34.4 12:22 33.7 13:32 32.3 11:13 35.2 12:23 33.1 13:33 32.4 11:14 34.2 12:24 32.8 13:34 31.4 11:15 33.9 12:25 32.4 13:35 32.5 11:16 35.0 12:26 33.5 13:36 31.7 11:17 36.1 12:27 32.9 13:37 31.5 11:18 35.9 12:28 33.0 13:38 30.7 11:19 35.4 12:29 34.2 13:39 31.6 11:20 35.3 12:30 34.0 13:40 31.2 11:21 35.0 12:31 33.0 13:41 31.7 11:22 34.5 12:32 33.3 13:42 30.9 11:23 35.2 12:33 33.2 13:43 30.3 11:24 35.1 12:34 33.7 13:44 31.4 11:25 35.4 12:35 34.0 13:45 31.0 11:26 34.4 12:36 33.5 13:46 30.9 11:27 34.5 12:37 32.8 13:47 31.2 11:28 35.1 12:38 33.5 13:48 32.6 11:29 34.7 12:39 33.0 13:49 32.7 11:30 34.9 12:40 32.3 13:50 31.9 11:31 35.0 12:41 32.8 13:51 33.1 11:32 35.5 12:42 33.3 13:52 31.8 11:33 36.1 12:43 33.5 13:53 32.0 11:34 35.9 12:44 33.9 13:54 31.6 11:35 34.0 12:45 34.6 13:55 32.0 11:36 33.9 12:46 33.2 13:56 31.6 11:37 34.3 12:47 32.7 13:57 31.5 11:38 34.8 12:48 34.0 13:58 30.8 11:39 35.7 12:49 33.4 13:59 30.6 11:40 34.9 12:50 33.8 14:00 31.5 11:41 34.7 12:51 33.1 14:01 31.9 11:42 34.6 12:52 33.1 14:02 31.7 11:43 33.9 12:53 33.1 14:03 31.5 11:44 34.2 12:54 32.4 14:04 31.7 11:45 34.8 12:55 33.4 14:05 32.6 11:46 34.8 12:56 34.2 14:06 32.3 11:47 34.8 12:57 33.7 14:07 31.4 11:48 34.5 12:58 33.7 14:08 32.6 11:49 34.0 12:59 32.9 14:09 31.8 11:50 34.8 13:00 33.0 14:10 31.7 11:51 34.2 13:01 34.2 14:11 30.9

.

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

### --------------_. MAX : 36.1 MAX : 34.6 MAX : 33.2 MIN: 33.4 MIN: 31.9 MIN: 30.3 AVG: 34.7 AVG: 33.2 AVG: 31.9 SCANS: 60 SCANS: 60 SCANS: 60


# :106SV030 SV030 SV030 Run 1 Run 2 Run 3 Date: 5/8/07 Date: 5/8/07 Date: 5/8/07 NOX NOX NOX Time PPM Time PPM Time PPM
._--------------- ----------------- ._------------- 7:08 47.7 8:19 48.1 9:32 48.7 7:09 45.5 8:20 48.3 9:33 48.5 7:10 49.0 8:21 48.7 9:34 48.7 7:11 49.5 8:22 48.6 9:35 51.8 7:12 50.4 8:23 47.3 9:36 49.5 7:13 48.8 8:24 50.2 9:37 49.3 7:14 48.9 8:25 48.2 9:38 49.4 7:15 48.3 8:26 51.0 9:39 50.4 7:16 49.3 8:27 51.4 9:40 48.2 7:17 50.2 8:28 49.2 9:41 48.9 7:18 49.7 8:29 50.2 9:42 49.4 7:19 48.9 8:30 51.2 9:43 49.4 7:20 48.0 8:31 49.8 9:44 49.9 7:21 49.5 8:32 50.2 9:45 48.6 7:22 50.0 8:33 49.5 9:46 49.4 7:23 51.5 8:34 49.0 9:47 48.1 7:24 47.2 8:35 49.7 9:48 49.7 7:25 49.5 8:36 49.7 9:49 48.6 7:26 50.8 8:37 47.8 9:50 49.6 7:27 49.3 8:38 50.5 9:51 48.9 7:28 48.2 8:39 50.7 9:52 49.4 7:29 47.6 8:40 50.7 9:53 50.1 7:30 48.9 8:41 50.7 9:54 49.8 7:31 47.4 8:42 50.7 9:55 49.9 7:32 49.1 8:43 51.2 9:56 48.6 7:33 49.7 8:44 49.2 9:57 48.9 7:34 47.9 8:45 50.9 9:58 . 51.0 7:35 50.0 8:46 50.7 9:59 50.8 7:36 48.4 8:47 49.8 10:00 49.7 7:37 48.4 8:48 50.0 10:01 48.8 7:38 48.0 8:49 49.3 10:02 49.7 7:39 49.0 8:50 47.7 10:03 50.2 7:40 47.9 8:51 48.7 10:04 50.5 7:41 47.5 8:52 48.5 10:05 49.6 7:42 47.4 8:53 49.2 10:06 50.0 7:43 47.2 8:54 49.5 10:07 50.6 7:44 46.5 8:55 49.8 10:08 47.5 7:45 46.9 8:56 48.2 10:09 48.3 7:46 47.0 8:57 47.8 10:10 48.6 7:47 49.7 8:58 44.6 10:11 49.7 7:48 47.1 8:59 42.7 10:12 49.9 7:49 47.3 9:00 40.7 10:13 49.0 7:50 46.2 9:01 41.0 10:14 49.4 7:51 43.6 9:02 40.0 10:15 48.9 7:52 44.8 9:03 41.4 10:16 49.9 7:53 46.0 9:04 42.2 10:17 49.3 7:54 45.4 9:05 42.7 10:18 49.5 7:55 46.5 9:06 43.7 10:19 50.1 7:56 43.7 9:07 44.9 10:20 51.0 7:57 44.7 9:08 45.8 10:21 50.5 7:58 43.5 9:09 45.0 10:22 51.2 7:59 42.9 9:10 46.2 10:23 50.1 8:00 43.2 9:11 46.3 10:24 51.3 8:01 41.7 9:12 47.1 10:25 51.4 8:02 43.6 9:13 45.2 10:26 50.8 8:03 45.0 9:14 46.1 10:27 49.1 8:04 44.7 9:15 45.8 10:28 48.7 8:05 45.2 9:16 43.2 10:29 49.0 8:06 43.2 9:17 41.9 10:30 49.8 8:07 44.2 9:18 42.9 10:31 50.4

----------------- 

### ----------------- ------------ MAX : 51.5 MAX : 51.4 MAX : 51.8 MIN: 41.7 MIN : 40.0 MIN : 47.5 AVG: 47.3 AVG: 47.5 AVG: 49.6 SCANS: 60 SCANS: 60 SCANS: 60SV031 SV031 SV031 Run 1 Run 2 Run 3 Date: 5m07 Date: 518107 Date: 518107 

### NOX NOX NOX Time 

### PPM Time 

### PPM Time 

### PPM

----------------- ----------------- -------------- 17:00 71.5 6:11 71.5 7:38 70.0 17:01 67.7 6:12 70.9 7:39 70.8 17:02 70.4 6:13 66.3 7:40 72.0 17:03 69.7 6:14 67.6 7:41 66.3 17:04 71.8 6:15 67.1 7:42 71.2 17:05 66.8 6:16 69.5 7:43 67.7 17:06 66.5 6:17 66.1 7:44 67.6 17:07 70.1 6:18 66.9 7:45 69.4 17:08 67.4 6:19 70.7 7:46 69.7 17:09 66.8 6:20 71.2 7:47 69.6 17:10 68.3 6:21 67.4 7:48 66.7 17:11 70.3 6:22 71.6 7:49 71.9 17:12 68.2 6:23 67.7 7:50 67.3 17:13 69.7 6:24 66.0 7:51 69.0 17:14 67.9 6:25 66.5 7:52 67.6 17:15 71.4 6:26 71.0 7:53 71.9 17:16 69.1 6:27 66.3 7:54 70.4 17:17 70.4 6:28 70.4 7:55 71.4 17:18 66.2 6:29 67.2 7:56 71.1 17:19 70.8 6:30 67.3 7:57 68.4 17:20 70.0 6:31 67.1 7:58 66.7 17:21 71.5 6:32 66.2 7:59 68.7 17:22 68.2 6:33 66.0 8:00 69.2 17:23 67.3 6:34 68.0 8:01 67.9 17:24 71.5 6:35 66.3 8:02 70.7 17:25 67.8 6:36 71.2 8:03 66.3 17:26 68.2 6:37 71.8 8:04 67.0 17:27 66.8 6:38 66.1 8:05 66.1 17:28 69.8 6:39 71.7 8:06 69.9 17:29 70.5 6:40 67.8 8:07 67.3 17:30 67.6 6:41 67.8 8:08 67.1 17:31 68.1 6:42 70.3 8:09 71.3 17:32 71.7 6:43 71.9 8:10 66.4 17:33 71.5 6:44 70.6 8:11 69.2 17:34 69.5 6:45 69.6 8:12 68.2 17:35 67.6 6:46 70.5 8:13 69.3 17:36 72.0 6:47 70.8 8:14 70.4 17:37 70.7 6:48 66.9 8:15 69.4 17:38 67.2 6:49 69.4 8:16 68.5 17:39 69.2 6:50 67.5 8:17 70.4 17:40 68.4 6:51 67.0 8:18 68.3 17:41 71.4 6:52 68.6 8:19 69.1 17:42 67.1 6:53 69.5 8:20 69.7 17:43 66.9 6:54 67.5 8:21 67.7 17:44 70.8 6:55 66.0 8:22 70.8 17:45 66.6 6:56 66.4 8:23 66.2 17:46 68.0 6:57 67.1 8:24 67.2 17:47 71.8 6:58 66.9 8:25 66.4 17:48 67.8 6:59 66.9 8:26 67.1 17:49 69.2 7:00 68.6 8:27 68.6 17:50 72.0 7:01 69.2 8:28 69.0 17:51 71.5 7:02 68.8 8:29 71.0 17:52 71.2 7:03 68.8 8:30 67.2 17:53 69.8 7:04 68.7 8:31 66.4 17:54 67.5 7:05 67.3 8:32 67.4 17:55 68.6 7:06 70.1 8:33 70.1 17:56 69.3 7:07 69.2 8:34 69.7 17:57 71.5 7:08 71.4 8:35 66.9 17:58 71.7 7:09 68.6 8:36 69.3 17:59 66.2 7:10 71.2 8:37 66.6 

### MAX : 72.0 

### MAX : 71.9 

### MAX : 72.0 

### MIN : 66.2 

### MIN : 66.0 

### MIN : 66.1 AVG: 69.3 AVG: 68.6 AVG: 68.7 

### SCANS: 60 

### SCANS: 60 

### SCANS: 60SV032 SV032 SV032 Run 1 Run 2 Run 3 Date: 5m07 Date: 5m07 Date: 5/8/07 NOX NOX NOX Time PPM Time PPM Time PPM 

### -_._._----------- ._-.----.--------- ._------------_. 14:22 99.9 15:39 96.5 5:55 100.9 14:23 99.5 15:40 96.6 5:56 100.9 14:24 98.5 15:41 99.3 5:57 101.3 14:25 96.4 15:42 97.2 5:58 102.0 14:26 96.0 15:43 95.3 5:59 101.2 14:27 100.7 15:44 96.5 6:00 102.4 14:28 100.6 15:45 97.5 6:01 102.1 14:29 98.4 15:46 97.6 6:02 102.8 14:30 96.4 15:47 99.2 6:03 102.0 14:31 93.9 15:48 95.4 6:04 101.6 14:32 94.8 15:49 96.7 6:05 100.5 14:33 98.6 15:50 96.7 6:06 102.1 14:34 101.5 15:51 97.0 6:07 101.2 14:35 103.3 15:52 97.2 6:08 103.5 14:36 99.2 15:53 98.9 6:09 102.4 14:37 104.0 15:54 97.7 6:10 106.0 14:38 99.7 15:55 97.2 6:11 103.5 14:39 101.3 15:56 96.7 6:12 100.8 14:40 99.5 15:57 95.7 6:13 101.9 14:41 102.1 15:58 94.2 6:14 106.3 14:42 102.6 15:59 97.2 6:15 108.5 14:43 100.5 16:00 99.0 6:16 104.1 14:44 102.1 16:01 97.7 6:17 105.4 14:45 102.3 16:02 96.5 6:18 103.1 14:46 100.2 16:03 99.0 6:19 101.6 14:47 98.3 16:04 97.0 6:20 101.3 14:48 98.1 16:05 98.4 6:21 102.7 14:49 96.8 16:06 98.9 6:22 106.0 14:50 100.2 16:07 99.9 6:23 101.3 14:51 99.9 16:08 96.8 6:24 105.6 14:52 100.4 16:09 97.1 6:25 101.3 14:53 99.9 16:10 97.1 6:26 103.5 14:54 100.2 16:11 99.5 6:27 102.9 14:55 102.1 16:12 96.9 6:28 102.1 14:56 99.9 16:13 100.9 6:29 103.5 14:57 99.3 16:14 99.4 6:30 100.5 14:58 103.1 16:15 99.9 6:31 101.3 14:59 101.2 16:16 97.5 6:32 105.3 15:00 102.0 16:17 97.5 6:33 102.7 15:01 100.3 16:18 96.0 6:34 104.1 15:02 102.0 16:19 92.6 6:35 102.2 15:03 100.2 16:20 95.4 6:36 103.6 15:04 101.1 16:21 94.9 6:37 101.4 15:05 96.9 16:22 96.1 6:38 101.7 15:06 96.8 16:23 98.6 6:39 101.9 15:07 98.3 16:24 95.3 6:40 103.9 15:08 98.3 16:25 95.1 6:41 105.2 15:09 101.0 16:26 94.9 6:42 105.2 15:10 98.9 16:27 93.7 6:43 105.0 15:11 96.6 16:28 97.0 6:44 101.4 15:12 97.1 16:29 96.4 6:45 103.6 15:13 98.6 16:30 95.9 6:46 105.0 15:14 98.8 16:31 94.7 6:47 104.4 15:15 95.9 16:32 95.0 6:48 104.6 15:16 95.9 16:33 94.9 6:49 103.5 15:17 96.6 16:34 96.7 6:50 104.2 15:18 93.8 16:35 96.1 6:51 106.9 15:19 95.6 16:36 94.5 6:52 103.7 15:20 96.5 16:37 91.5 6:53 103.5 15:21 95.8 16:38 96.6 6:54 104.1

----------------- 

### ----------------- ._--------------- MAX : 104.0 MAX : 100.9 MAX : 108.5 MIN : 93.8 MIN : 91.5 MIN : 100.5 AVG: 99.1 AVG: 96.8 AVG: 103.1 SCANS: 60 SCANS: 60 SCANS: 60**,~** 

# 09**~,** 

### . 

# """"

....

### CALIBRATION ERROR SUMMARY METHODS 3A, GC, 7E, 10 

### & 25A

Job Number: Company: Plant: Test Location:

, " "

,

### ""\ ",

## .. "" ,

### Anai#~r",·" " 

### ,,",'.,'.' I 

# Pollutant "

### ... '.:" 

# "

",' "

## Ma~ufacttlrer ",',.,1 '. , 

## ,.,,"**I\IId~eINo.** 

# .**;'·,S~rial** 

# No.}} ,',

" " ',,'.**-~>.** 

### O2 

# .5 e-...

# m-« J

## YIJI) 

## 2ttJ I

## If/(} CO2 5l-l"tH"'-"" 

## /'1&0 'J..,,(/O It/i/O 

### 802 

### NOx 

# jEt-cf) 'ilL 'Lfl£/J/-7!J7H1-37f 

# co THC

02 Zero 

## AL/IIIlJlS"J7J**(·/~·O'6** Mid 

# AlMU'rSO 

# J- 1.)

- 

### loi()



### C02 Zero 

# IJ 

# 5L f"J.

# C'17 Mid 

# !JLMl.oW High 

# JJ

# 1/1 J

# 6J ) I 802 Zero ./ 

# - 6-3- /J 7

NOx

CO Mid High Zero Low turbines only 

### Mid High Zero Low Mid High 

# Ai /lOU'1

# s»
A

1/'1 Jb J ) / (,-)3-/7 

# G

... )-/7 

# )"-1)-01 

# o 1/1, (

THC Zero Low Mid High

Note: For all CO and THC sampling, and for all sampling performed on Gas Turbines, all calibration gases are sent through the entire sampling system, not directly to the analyzer.

### CALIBRATION DRIFT 

### & SYSTEM BIAS SUMMARY METHODS 3A, GC, 7E, 10 

### & 25A
O2 

### CO2 

### 802 

### NOx 

### CO ,.- 

### VOC Analyzer Span: Analyzer Response to Zero*: 

### N/A N/A Analyzer Response to Upscale*: 

### N/A N/A System Zero 

# b,O 0,0



# - o. '-I System Upscale

### ~I. 

## 4 1/ 0 

# rus:« t,}3/ 

## -7:11 'U/I 

# IJ."**57.~** 

# I System Zero 

## O,b 

# 6,/ -0, JSystem Upscale 

## 'lA.1i 

# '1 '2.

## /11.

# f )

, 

## '7 

# :.,6 

# -**~:ljO** 

### ':).,0.3 

# d. l.f 

# e,-t. 'i System Zero (J,

## 0 

## O. I**~d** System Upscale

### v.~ 

# II 'lU. I 

# q

# 0"'- -/{):6'5 

## 2.1.0 

# i« cs.o System Zero 

# 0.0 U; I 

## - (1.3 System Upscale 

## ) o ?, 

# 11 1.

# /6. 1**~O** '.1.,1)

- 

# 11:'lr 

# ¥/C"b :IS f), 

## 7 (1/. ( System Zero (J,g 

# 0, , ,- 0, 

## .3 System Upscale 

## n», (1 

# II ll( 

# '5 1/:4:3- 

# n: 1./3 

# n.«: IJ. 7 q'), 

## 7 System Zero 

## C'J}**O~** 

# , -f P,

## 7 System Upscale 

### 2b,**~i** 

# I 2./( 0 

## 11: 

# ')7

- 13**.~r;7** 

## /1.**~-** "lIe;- 

### ()(2J..Y**fJ~./4t'~** System Zero 

## d.i! 1 0.41 System Upscale 

# ·to. q 'I,),a 

## J.I

# '-(.Ii

# t 

# / iLl: 

## /3

- 

# t«: 13 1t1f, lt1X .'/R 

## d.**7/~ ,~**  /()) 

# 111:J "7 System Zero 

### IINLI 

# () c 'j 

### 'I -, Z**7~** i System Upscale 

## 1-0,**f~** 

### J 

## 0, iJ'C' 'l/). 

# 17 ')'16" - 

# ''1b /4:2.. 

# .J::!i:;:t I. 7 

### ;,):J3. 'of OJf

# .rr System Zero (),d t- 

### Il. (**~(J,3** System Upscale 

### '2,.CI,

# s**/l~** 4;::1:SI-'2 J1, " 

# 0100

- 0'1,(;; 

### /If 

# tI 7**~--4** System Zero 

### 0./)0 

### 6,( -()•..3 System Upscale 

## 'UI.4' 

## Jl 1**~,** 

### :J..,1j 

## {}i:37-lJq**~7** 

## 1 II. '- 

# 11. 7 1tJ2.7{ System Zero 

## lJ,tJ 1 

# I.**(;~** 

## J/J.q'j System Upscale 

### LI, Ii 

# " 0 ... IL1-f 

# 'l 10 :&11

- 

# 11'[,11- Ifi.H7 

# 0, 7ft('" 1() 7.

# a System Zero 

# fl.'" fI,I7**~. 7~2.**  System Upscale 

## .2. "

## i .,- nOI '2.(

## }:j 

# 11 :tJ7

- 

# 1<.: ')7· I

# Ii l (J ., 

## " 3.l System Zero 

## D,**~,** 

## h.OD - II 

# J System Upscale

### ~~I.o 

## /1/, ., 

# "1..1',-, 'f & 

# 5VOll

5VOlj

* Not applicable for O2, 

### CO2

# OJ' NOx 

### on Turbines. Acceptable system response for O2, 

### CO2, 

### 802 

### or NOx

### (non-turbine applications): analyzer response 5% of span Acceptable system response for O2, 

### CO2, 

### & NOx 

### on turbines, and CO in all applications: 2% of span Acceptable system response for VOC: 5% of gas value Acceptable system drift for O2, 

### CO2, 

### 802 

### or NOx

### (non-turbine applications): 3% of span Acceptable system drift for O2, 

### CO2 

### or NOx

### on turbines: 2% of span Acceptable system drift for CO: 10% of span in 8 hours Acceptable system drift for VOC: 3% of span

### CALIBRATION DRIFT 

### & SYSTEM BIAS SUMMARY METHODS 3A, GC, 7E, 10 

### & 25A
O

### 2 CO

### 2 802 NOx 

### CO VOC Analyzer Span: Analyzer Response to Zero*: 

### N/A N/A Analyzer Response to Upscale*: 

### N/A N/A System Zero 

# 6 '\ (**O,~'"** - (I, 

## 'J System Upscale 

### "l.f.t\ 

### 10. -, 

# t«

# s«

# ~j ,": If- , lM'1 jq,c; IJ. 

# "q 

# 104. 1tt System Zero 

### 1.66 I/J). 

# - o, '3 System Upscale 

## ,,1 I Ilf «4 

# "lot', 141':11

.. 

# J,5"; ")''- 14/1f 

# 0.,1 10'1,'1'1 System Zero 

### () tJ 

### -0•

## .3 

# f -OJ-oK.. System Upscale 

## 'U.4 11, , '2.)..0,

## q 

# 66'J

## '117

- 

# 0&I.f<' 

# 111.1." 0/,[7 

# e«. f).. System Zero 

### d. fJ

## '1 ().6' f),Qf' System Upscale 

## t-j f

## r' ID:iffl ").1&.' ';1 

# 07lit ,. 

# a'III /4.411 

## O. )If**~'l;y** System Zero 

## //.0' -;(Jl.. 

# aq System Upscale 

## '10.4 , 

# I(J. If

# '1 '2

## It, (

# )'V017~**d~:/:l-** 

# ":t3 I 

## "I, 9) 

## d, ::J

## LI ,'., C System Zero 

### Ii f)

### l.f7 

## 6 lJf:J 

### -0,1J System Upscale 

### '}..Q.76 

# u. 'it**ll,ff~** 

### OQ';Jl- 

# to :j.J 

# Iq,ld 0. 

## '??"t £7.2.'1 System Zero 

## II. fJ

# 7 

# a,»a**-~,JJ** System Upscale 

## 2.8, f1.'- 

## 1/,0'1 2/'(.111 

# ( III If' 

# 4 - 11 

## ')I.f**'"L4.~** 

## 11. )...

# '6 }l.OJI System Zero 

## 0, (.,''1 1/,/1 

# 6e..Jr 

# J'V01l1 System Upscale 

### ":l(),. 

### Ci7 

## -0 

# ia , '"1.((. 

## q

# '1 11 '10

- '310 '1-.0, 

## J... a'")**~-:2.:J** System Zero 

## £t.

# o'7 

## 'f &, 

## -1'1 ---1/.

# o1.,(/

# '6 ;'O!.J.IJ 

# l System Upscale 

### J.Jj, 

## q

# Lf**~I** I, 

## • II. 

## I 'lJ 1. 

# qt IJ:2,&

- 

# 142' ').Or ( 

# ., 1

" 

# r-J61 System Zero 

# ovL1Ji; -f1 

## 0:[ 

## --0.

# 1." System Upscale

### '1~ 

### t;

# 16 II, {; 

# 6(, 

# :). n t1 

# / System Zero System Upscale



# ...

# '''~ System Zero System Upscale
System Zero System Upscale



### * 

### Not applicable for 

### 02, CO

### 2or NOx

### on Turbines. Acceptable system response

## for 02, CO

### 2 , 802or NOx

### (non-turbine applications): analyzer response 

## ± 5% of span Acceptable system response for O2, 

### CO2, 

### & NOx 

### on turbines, and CO in all applications: 

## ±2% of span Acceptable system response for VOC: 

# .± 5% of gas value Acceptable system drift for 

### 02, CO

### 2 , 802or NOx

### (non-turbine applications): 

## ± 3% of span Acceptable system drift for 

### 02, CO

### 2or NOx

### on turbines: 

## ±2% of span Acceptable system drift for CO: 

# .± 10% of span in 8 hours Acceptable system drift for VOC: 

# .± 3% of span

### CALIBRATION DRIFT 

### & SYSTEM BIAS SUMMARY METHODS 3A, 6C, 7E, 10 

### & 25A
O2 

### CO2 

### 802 

### NOx 

### CO VOC Analyzer Span: Analyzer Response to Zero': 

### N/A N/A Analyzer Response to Upscale': 

### N/A N/A System Zero 

# -I, ( 

# o.( I. 

# I 

# '#7/ System Upscale 

### {( 

# 1#. llJ,."" J

## Lf**~~** 

## ... (.,'J.. 

### .2- 

# (j.b bit,'**'1~.1** System Zero 

# -# 

# O·b 

# o.o I. .., System Upscale 

## fA U. , J.1'1.7



# t« )'J

...**I(')~** 

# Oc 1'1

.. 

# 2 tilO System Zero 

## "# 

# 0.0

- f). ( 

# .7 System Upscale 

## "1:t • ., 

# \." '1.(1), 

# 1 

# 7 Or**~'i** 

# - 

# vC 51**'~,1J..'i** 

# (J.t,36 

# MJ./2.' System Zero 

# V 

# o.n (j.6 .7 System Upscale 

# /1 

# o...r.rJ 

# 1.'7

.. 1 / 

### /j

# 7 U'fJ 

# - n«**v~ ~J**  

# G.) '17

.." System Zero 

### ().{) 

# O,u 

# D. 7 System Upscale 

## :l 

# 1.0 I, I 

## 'll?,) 

# )0..1 H 11 -)t::f1f "'1 

## 11 

# "'.1- 1i.':J 

# 1.(7, 

# if System Zero 

# 0.0 0.1 

# 0.' System Upscale 

# '1.r., II. (J 

## 217.

# e; -, q:')2-IO:1<" 

# .16

..

# 1.. 6.,\ &(4,6 System Zero 

# o.( nD 

# 0.' System Upscale 

## "l..1, f 

# h' :L "'

..f)



# ... ; 

### -, System Zero System Upscale



# IlJ:'-'1.

...**'f~.IJ~**

### ~.'1 

## d./ '"\ 1./. 

## ? System Zero**p.~** 

## 1i.1 

## IJ. , System Upscale 

## ),,1**~II** 

## (f, () 

## 'l..lJ. ) 

# /1.:**()'L-r~:!l)"** 

# 1..tJ4 

# (J.t**~J.** 

## J.. System Zero (f.

## I> -//,f 

## Ii ) System Upscale 

# Vq 

# t-fJ.' '). :a.

# 2.::1"**I~** 

## 11- 11,.f-/

# a, 

# U/;'t 8,1 "11 

## 4 System Zero 

# 0,0**!J.~** 

# 0.7 System Upscale 

# 'VA U,1**~~** System Zero System Upscale
System Zero System Upscale 

# r/7/t

* Not applicable for O2, 

### CO2 

### or NOx

### on Turbines.

j 

### Acceptable system response for O2, 

### CO2, 

### 802 

### or NOx

### (non-turbine applications): analyzer response j, 

### 5% of span Acceptable system response for O2, 

### CO2, 

### & NOx

### on turbines, and CO in all applications: 

# .±. 2% of span Acceptable system response for VOC: 

# .±. 5% of gas value Acceptable system drift for O2, 

### CO2, 

### 802 

### or NOx

### (non-turbine applications): 

# .±. 3% of span Acceptable system drift for O2, 

### CO2 

### or NOx

### on turbines: 

# .±. 2% of span Acceptable system drift for CO: 

# .±. 10% of span in 8 hours Acceptable system drift for VOC: 

# .±. 3% of span 

# i(13

## 27.7 173.0 216.4 217.4 225.2 219.0 218.7 218.4 217.9 218.2 217.8 . 192.7 1.8 0.3 0.3 0.3 22.4

3.1 13.3

0.3 0.3 0.3 0.3 0.3 0.3 295.2 420.5 421.1 419.7 415.9 416.2 415.8 328.3 814.1 827.1 828.7 828.9 831.4 831.0 367.9

12.6

1.5 1.3 1.3 1.3 18.5 33.5 11.6

1.3 SV021 Initial Linearity NOx 

## 5:26 5:27 5:28 5:29 5:30 5:31 5:32 5:33 5:34 5:35 5:36 5:37 5:38 5:39 5:40 5:41 5:42 5:43 5:44 5:45 5:46 5:47 5:48 5:49 5:50 5:51 5:52 5:53 5:54 5:55 5:56 5:57 5:58 5:59 6:00 6:01 6:02 6:03 6:04 6:05 6:06 6:07 6:08 6:09 6:10 6:11 6:12 6:13 6:14

### Pre Rn 1 NOx 

## 6:16 1.3 6:17 1.3 6:18 1.3 6:19 0.9 6:20 0.3 6:21 1.2 6:22 1.3 6:23 1.3 6:24 74.2 6:25 195.2 6:26 196.7 6:27 213.4 6:28 223.9 6:29 218.9 6:30 187.9



# 115

## SV022 Initial Linearity

---------------- 

## NOX2 Time 

# PPM

---------------- 

## 5:26 44.4 5:27 156.9 5:28 163.9 5:29 190.9 5:30 217.9 5:31 217.9 5:32 217.9 5:33 217.9 5:34 217.9 5:35 217.9 5:36 217.9 5:37 200.2 5:38 74.4 5:39 -0.2 5:40 -0.4 5:41 -0.4 5:42 4.3 5:43 12.8 5:44 18.5 5:45 -0.4 5:46 -0.4 5:47 1.8 5:48 -0.4 5:49 -0.4 5:50 -0.2 5:51 269.0 5:52 421.4 5:53 420.9 5:54 418.6 5:55 417.1 5:56 417.3 5:57 416.7 5:58 479.7 5:59 817.7 6:00 831.5 6:01 832.5 6:02 833.4 6:03 834.3 6:04 818.7 6:05 680.5 6:06 35.7 6:07 1.3 6:08 0.7 6:09 0.1 

# 116

## 6:10 -0.4 6:11 16.1 6:12 72.4

Pre Rn 1 Time NOx 

## 6:16 -0.4 6:17 -0.4 6:18 -0.4 6:19 -0.4 6:20 -0.3 6:21 -0.4 6:22 -0.3 6:23 -0.3 6:24 57.9 6:25 213.9 6:26 215.9 6:27 215.9 6:28 215.9 6:29 215.9 6:30 187.9

Pre Rn 2
NOX2 Time PPM


## 7:37 208.1 7:38 214.9 7:39 214.9 7:40 142.2 7:41 1.0 7:42. .**~O.2** 

## 7:43 8.2 7:44 172.6
Pre Rn 3
NOX2 Time PPM


## 8:54 215.9 8:55216.1 8:56 216.1 8:57 188.5 8:58 2.1 8:59 -0.1 9:00 27.7

## 9:01 149.4

Post Rn 3
NOX2 Time 

### PPM


## 10:09 216.6 10:10 216.8 10:11 216.1 10:12 216.3 10:13 107.2 10:14 0.7 10:15 -0.1 10:16 -0.3 10:17 -0.3 10:18 ;.0.3 10:19 -0.3 10:20 -0.3



# 1.1.8

## SV023 Pre Rn 1
NOX2 

### Time PPM


## 10:09 216.6 10:10 216.8 10:11 216.1 10:12 216.3 10:13 107.2 10:14 0.7 10:15 -0.1 10:16 -0.3 10:17 -0.3 10:18**~0.3** 

## 10:19 -0.3 10:20 -0.3

Pre Rn 2
NOX2 

### Time PPM


## 11:29 181.6 11:30 217.0 11:31 216.9 11:32 216.8 11:33 216.8 11:34 216.8 11:35 167.7 11:36 3.4 11:37 0.5 11:38 -0.3 11:39**~0.3** 

## 11:40 -0.3 11:41 127.0

Pre Rn 3 NOx 

## 12:47 91.9 12:48 136.9 12:49 216.0 12:50 215.9 12:51 215.9 12:52 76.8 12:530.7 12:54 2.1



# :11.9

### Post 3
NOX2 Time PPM


## 14:00 140.3 14:01 215.0 14:02 214.8 14:03 214.8 14:04 215.0 14:05 214.7 14:06 208.6 14:07 39.5 14:08 0.7 14:09 0.4 14:10 -0.3 14:11 -0.3

### SV024 Pre Rn 1
NOX2 Time PPM



## ---------------- 14:00 140.3 14:01 215.0 14:02 214.8 14:03 214.8 14:04 215.0 14:05 214.7 14:06 208.6 14:07 39.5 14:08 0.7 14:09 0.4 14:10 -0.3 14:11 -0.3

Post Rn 1

NOX2 Time PPM



## ---------------- 15:15 214.4 15:16 214.0 15:17 214.0 15:18 214.0 15:19 189.4 15:20 1.5 15:21 0.7 15:22 0.2 15:23 -0.3 15:24 -0.3

Linearity 05-02-07
NOX2 Time PPM



## ------------------- 5:15 -0.3 5:16 180.7 5:17 232.9 5:18 232.3 5:19 231.9 5:20 227.5 5:21 217.9 5:22 217.0

### 5:23 166.2 5:24 37.8 5:25 17.6 5:26 3.8 5:27 -0.3 5:28 0.2 5:29 337.0 5:30 417.8 5:31 418.0 5:32 417.4 5:33 411.1 5:34 119.8 5:35 0.7 5:36 0.3 5:37 -0.3

Pre Rn 2
5:37**~0.3** 

### 5:38 15.0 5:39 92.4 5:40 89.1 5:41 178.8 5:42 212.9 5:43 213.3 5:44 213.9 5:45 191.7

Pre Rn 3
NOX2 Time PPM



## ------------------- 6:49 92.3 6:50 191.7 6:51 212.9 6:52 171.6 6:53 4.3 6:54 0.7 6:55 -0.3 6:56 -0.3 6:57 118.2 6:58 104.5

Post Rn 3
NOX2 Time PPM



## ------------------- ,'1**~"J2** 

### .A.S!W

## 8:00 89.5 8:01 108.8 8:02 211.9 8:03 217.6 8:04 217.8 8:05 217.7 8:06 160.8 8:07 1.9 8:08 0.0 8:09 -0.3 8:10 -0.3 8:11 -0.3



# .1.23

## SV025 Pre Rn 1

NOX2 

### Time PPM


## 8:00 89.5 8:01 108.8 8:02 211.9 8:03 217.6 8:04 217.8 8:05 217.7 8:06 160.8 8:07 1.9 8:08 0.0 8:09 -0.3 8:10 -0.3 8:11 -0.3

Pre Rn 2
NOX2 

### Time PPM


## 9:37 105.7 9:38 106.9 9:39 114.5 9:40 210.2 9:41 212.9 9:42 212.9 9:43 212.9 9:44 135.7 9:45 0.7 9:46 0.7 9:47 -0.1 9:48 -0.3 9:49 -0.3 9:50 -0.3 9:51 -0.3 9:52 -0.3

Pre Rn 3

NOX2 

### Time PPM


## 11:46 159.1


# :124

## 11:47 215.2 11:48 215.0 11:49 215.6 11:50 215.3 11:51 176.5 11:52 58.1 11:53 0.7 11:54 0.7 11:55 0.7 11:56 20.9

Post Rn 3
NOX2 Time PPM


## 12:57 117.1 12:58 111.6 12:59 198.2 13:00 212.0 13:01 212.7 13:02 216.0 13:03 216;0 13:04 112.8 13:05 30.0 13:06 1.3 13:07 0.4 13:08 -0,3 13:09 25.0



# 1.25

### Pre Rn 1

NOX2 Time PPM
12:57 117.1 12:58 111.6 12:59 198.2 13:00 212.0 13:01 212.7 13:02 216.0 13:03 216.0 13:04 112.8 13:05 30.0 13:06 1.3 13:07 0.4 13:08 -0.3 13:09 25.0

Pre Rn 2



## ------------------- NOX2 Time PPM



## ------------------- 14:19 225.0 14:20 223.3 14:21 216.0 14:22 216.8 14:23 217.0 14:24 205.9 14:25 74.3 14:26 -0.1 14:27 -0.3 14:28 -0.3 14:29 -0.3 14:30 55.7 14:31 94.5 14:32 108.8

Post Rn 2 NOX2 Time PPM



## ---------------- 15:36 208.9

## 15:37 220.7 15:38 220.9 15:39 221.0 15:40 221.0 15:41 109.3 15:42 0.1 15:43 -0.3 15:44 -0.3

Initial Linearity05-03-07
NOX2 

## Time PPM
5:16 156.1 5:17 249.9 5:18 232.0 5:19 . 217.9 5:20 211.8 5:21 52.7 5:22 -0.4 5:23 -0.4 5:24 -0.4 5:25 278.7 5:26 415.9 5:27 415.5 5:28 415.2 5:29 222.4 5:30 0.6 5:31 -0.1 5:32 "0.4 5:33 -0.4

Pre Rn 3
5:34 45.0 5:35 211.0 5:36 213.9 5:37 201.2 5:38 9.6 5:39 0.4 5:40 -0.4 5:41 77.2 5:42 207.0 5:43 117.9



# 1.27

### Post Rn 3
NOX2 Time PPM


## 6:48 213.4 6:49 215.9 6:50 215.9 6:51 216.0 6:52 214.9 6:53 103.2 6:54 12.8 6:55 0.6 6:56 . 0.1 6:57 6.0 6:58 61.7 6:59 63.8

## SV027 Pre Rn 1
NOX2 

### Time PPM


## 6:48 213.4 6:49 215.9 6:50 215.9 6:51 216.0 6:52 214.9 6:53 103.2 6:54 12.8 6:55 0.6 6:56 0.1 6:57 6.0 6:58 61.7 6:59 63.8

Pre Rn 2

NOX2 

### Time PPM


## 8:01 69.4 8:02 69.8 8:03 150.4 8:04 216.9 8:05 216.2 8:06 215.9 8:07 154.5 8:08 69.0 8:09 58.5 8:10 0.9 8:11 -0.4 8:12 52.6 8:13 66.1

Pre Rn 3
NOX2 

### Time PPM


## 9:17 68.9 9:18 140.7 

# 129

## 9:19 214.1 9:20 213.9 9:21 213.9 9:22 213.9 9:23 213.7 9:24 213.4 9:25 141.9 9:26 44.0 9:27 0.7 9:28 -0.3 9:29 3.4 9:30 56.1 9:31 62.9

Post Rn 3
NOX2 

### Time PPM


## 10:38 73.5 10:39 192.6 10:40 209.7 10:41 214:1 10:42 214.9 10:43 214.3 10:44 113.3 10:45 52.3 10:46 51.3 10:47 50.6 10:48 50.7 10:49 14.2 10:50 -0.3 10:51 -0.3 10:52 30.8 10:53 48.8

### SV028 Pre Rn 1
NOX2 Time PPM

------------------- 

### 10:38 73.5 10:39 192.6 10:40 209.7 10:41 214.1 10:42 214.9 10:43 214.3 10:44 113.3 10:45 52.3 10:46 51.3 10:47 50.6 10:48 50.7 10:49 14.2 10:50 -0.3 10:51 -0.3 10:52 30.8 10:53 48.8

Pre Rn 2
NOX2 Time PPM

---------------- 

### 11:57 98.7 11:58 217.3 11:59 217.4 12:00 217.0 12:01 216.9 12:02 211.8 12:03 57.8 12:04 0.7 12:05 0.4 12:06 -0.3 12:07 17.9

Pre Rn 3
NOX2 Time PPM



## ------------------- 13:10 53.3 13:11 52.6 13:12 119.2 13:13 218.3 13:14 218.0 

# :131.

### 13:15 218.0 13:16 218.0 13:17 128.0 13:18 0.4 13:19 -0.3 13:20 0.0 13:21 0.7

Post Run 3
NOX2 Time PPM



## ---------------- 14:26 53.9 14:27 54.3 14:28 51.9 14:29 52.3 14:30 121.7 14:31 218.1 14:32 217.9 14:33 217.8 14:34 112.9 14:35 51.8 14:36 11.9 14:37 -0.3 14:38 -0.3 14:39 -999.0



# :132

### SV029 Pre Rn 1
NOX1 Time 

# PPM
10:32 49.9 10:33 49.3 10:34 49.3 10:35 90.2 10:36 219.0 10:37 168.7 10:38 230.1 10:39 231.8 10:40 158.3 10:41 25.7 10:42 0.9 10:43 0.6 10:44 0.0 10:45 38.9

Pre Rn 2
NOX1 Time 

# PPM

------------- 11:52 35.0 11:53 0.7 11:54 0.7 11:55 72.5 11:56 224.4 11:57 230.1 11:58 221.7 11:59 222.3 12:00 222.4 12:01 166.1

Pre Rn 3
NOX1 Time 

# PPM

------------- 

### 13:02 32.1 13:03 32.9 13:04 221.9 

# :133

## 13:05 222.5 13:06 222.8 13:07 222.8 13:08 115.9 13:09 7.3 13:10 0.7 13:11 0.7 13:12 1.6

Post Rn 3
NOX1 Time PPM


## 14:12 32.3 14:13 31.6 14:14 148.2 14:15 219.2 14:16 220.2 14:17 220.8 14:18 220.7 14:19 213.0 14:20 53.8 14:21 1.3 14:22 0.7



# :134

## SV030 Pre Rn 1
NOX1 Time PPM


## 6:55 103.2 6:56 101.0 6:57 163.4 6:58 217.7 6:59 217.7 7:00 217.6 7:01 217.7 7:02 105.5 7:03 40.3 7:04 3.1 7:05 1.4 7:06 0.7 7:07 14.9 7:08 47.7

Pre Rn 2
NOX1 Time PPM


## 8:08 45.5 8:09 45.2 8:10 60.9 8:11 206.1 8:12217.7 8:13 214.3 8:14 89.5 8:15 7.9 8:16 0.7 8:17 17.2 8:18 48.0 8:19 48.1

Pre Rn 3
NOX1 Time PPM


## 9:19 43.1 9:20 43.0 

# :i35

### 9:21 48.3 9:22 225.6 9:23 222.0 9:24 217.9 9:25 187.9 9:26 29.1 9:27 0.9 9:28 0.6 9:29 0.6 9:30 3.5 9:31 41.4 9:32 48.7

Post Rn 3
NOX1 Time PPM



## ------------- 10:32 49.9 10:33 49.3 10:34 49.3 10:35 90.2 10:36 219.0 10:37 168.7 10:38 230.1 10:39 231.8 10:40 158.3 10:41 25.7 10:42 0.9 10:43 0.6 10:44 0.0 10:45 38.9



# :136

## SV031

NOX2 Time PPM


## 15:50 -0.3 15:51 0.0 15:52 -0.1 15:53 60.0 15:54 68.6 15:55 70.4 15:56 69.4 15:57 63.7 15:58 193.7 15:59 219.0 16:00 219.0 16:01 219.0 16:02 151.8 16:03 79.4

Day 2 Linearity:



## 6:36 0.0 6:37 -0.3 6:38 -0.3 6:39 -0.3 6:40 -0.3 6:41 -0.3 6:42 -0.3 6:43 -0.3 6:44 41.2 6:45 227.5 6:46 219.4 6:47 217.8 6:48 216.9 6:49 217.0 6:50 203.7 6:51 410.3 6:52 410.1 6:53 411.7 6:54 47.9 

# :137

## 6:55 152.5

Remote


## 6:56 0.8 6:57 0.2 6:58 130.5 6:59 212.1 7:00 212.1 7:01 215.8 7:02 216.9 7:03 177.6 7:04 72.7 7:05 73.6

5/7/2007
13:04 100.3 13:05 203.1 13:06 214.9 13:07 215.1 13:08 215.5 13:09 216.1 13:10 216.0 13:11 198.8 13:12 107.8 13:13 7.0 13:14 1.8 13:15 1.0 13:161.0 13:17 1.0

5/8/2007
8:31 69.7 8:32 68.6 8:33 69.2 8:34 109.8 8:35 212.4 8:36 219.9 8:37 219.6 8:38 219.9 8:39 200.4 8:40 5.9 8:41 1.6

## ~38

## 8:42 1.0



# 1.39

## SV032 Initial Linearity
NOX2 Time PPM


## 13:40 13:41 13:42 13:43 13:44 13:45 13:46 13:47 13:48 13:49 13:50 13:51 13:52 13:53 13:54 13:55 13:56 13:57 13:58

Time
Pre Rn 1 

## 89.5 87.3 87.5 107.5 233.6 230.1 218.2 126.9

0.9 0.6 0.7 48.0 406.7 326.1 4.0 1.6 0.7 0.7 26.8
NOX2 PPM



## 14:03 1.6 14:04 . 1.1 14:05 -0.8 14:06 148.6 14:07 99.8 14:08 115.2 14:09 212.2 14:10 179.4 14:11 2.7

Pre Rn 2 NOX2 Time PPM


## 15:24 100.2 15:25 96.4 15:26 107.7 15:27 201.9 15:28 212.7

## 15:29 212.7 15:30 211.8 15:31 191.3 15:32 81.8 15:33 2.2 15:34 1.7 15:35 1.7 15:36 1.4 15:37 1.5

Post Rn 2
NOX1 

## Time PPM


## 16:44 98.6 16:45 149.0 16:46 217.6 16:47 218.3 16:48 218.7 16:49 218.5 16:50 217.0 16:51 109.5 16:52 7.6 16:53 1.6 16:54 0.7 16:55 '07 16:56 -999.0

Initial Linearity05-08-07

NOX1 

## Time PPM


## 5:00 0.7 5:01 0.7 5:02 0.7 5:03 0.7 5:04 0.7 5:05 0.7 5:06 0.7 5:07 0.7 5:08 0.7 5:09 0.7 5:10 0.7 5:11 0.7 

# :141.

## 5:12 0.7 5:13 0.7 5:14 0.7 5:15 0.7 5:16 0.7 5:17 0.2 5:18 0.7 5:19 14.3 5:20 41.2 5:21 185.7 5:22 217.1 5:23 216.7 5:24 216.4 5:25 215.6 5:26 214.6 5:27 213.9 5:28 88.0 5:29 2.2 5:30 1.1 5:31 0.7 5:32 0;7 5:33 0.7 5:34 3.6 5:35 331.1 5:36 398.8 5:37 399.3 5:38 404.7 5:39 411.5 5:40 412.6 5:41 259.4 5:42 3.0

Pre Rn 3


## 5:42 3.0 5:43 1.7 5:44 1.3 5:45 241.3 5:46 142.0 5:47 277.6 5:48 216.7 5:49 216.7 5:50217.4 5:51 217.7 5:52 216.4 5:53 131.4 5:54 103.3 5:55 100.9



# :142

### Post Rn 3
NOX1 

### Time PPM


## 6:55 103.2 6:56 101.0 6:57 163.4 6:58 217.7 6:59 217.7 7:00 217.6 7:01 217.7 7:02 105.5 7:03 40.3 7:04 3.1 7:05 1.4 7:060.7 7:07 14.9 7:08 47.7



# :143

## Methods 2, 3 & 4 Field Data Sheet Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area: Pitot ID: Pitot Cp: Meter ID: Meter Y: Meter LlH@i: Operators: 

## t, ") /4j, 

### Run Number: 

# -4.-t--- Page 

### .L: of 

# .L. Date: 

# 6?-1-&'7 Pbar ("Hg): 

### 'VI.**t:~** 

### Pstatic ("H20): 

### ,. 

# ()£

Pre-Test Poot Leak Check:

# 8
Fail Post Test Pitot Leak Check: Fail

Time Port Point LlP ("H2O) 

### Ts (OF)**:_~rr"** 

# A I**.,~** 

# 41 1'J,("#f/ 

## 2**~7'1** 

# 4'J 3 

# •et> 

# 1 q., l.( 

# .qJ If

# '1 

# S 

# .qJ 4'1 ( 

# . q I 

# 1'( 7 

# •/1 () 

# q" '6 ,tfjJ 

# try 

# '1 ,16 1;'1 (U o 

# 1 I 

## If,,! tt 

# lip 

# If,! (1 

# ,'to 

# qt

,

Use Bwsand MW data from previous Run? Yes No Time Port Point LlP ("H2O) 

### Ts (OF) 

## G ( 

## , (1

# ~II 

# n... ,,7Q**~I** 

# .116 f1 Lr 

# 011.. 

# tiJ \ 

# .'L**J{~** 

### If" 

# 12 'i? "? 

# .f1 4.) 

# e ." 1..**~:J** 

# .q ') qlf r/ 

# ,f3**1~** 

## (( 

# If't 

# r3

.. ,1. 

# 71 erA 

# K/7

Time 

## Vm 

### (fe) Meter Meter Imp. Out**~H** 

### In (oF) Out (OF) (oF) ("H2O) 

# i"r t;'f

# 'lIs 7 

# 't2 L() 

# ca: 'l..'" 

# rts: £''1.. 

# 43 f!U- tt') &.(4 

# rv« 

# "'., "1"1 

# \ \ / (2". 

## 4., 

# f/-r 

# far tt) 

# 'fc ('fitif' 

# f'{7.C,J7 

# ", 'Ie Imp# Initial Final Net 

## 1 7**r~.1.** 

## ]Ifo ). 2 

# 7'1 I 

## f 

# -?,r--6 3

# '~f. If**!C~_I** 

### 4 

## tP.,.7 44(·\ Total Train**~I** 

### Bws: 

# rtlt

Form 1012 GE Energy

## Methods 2, 3 & 4 Field Data Sheet Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

# «. 7/

.. Pitot ID: Pitot Cp: Meter ID: Meter Y: Meter**~H@i:** 

### Operators: I. 

### 'If 

### Run Number:

## _~-=-- 

## _ Page 

## t of I 

### Date: - 

# 6'/;.Q7 Pbar ("Hg): I 

### Pstatic ("H20): 

## rtJ,

# £

Pre-Test Pitot Leak Check: 

### Fail Post Test Pitot Leak Check: 

### Fail

Time Port Point**~p** 

### ("H2O) 

### Ts (oF) 

# 7¢ ;t""/J 

# , II&J

## 1~ f2...



# ...

# ), Ii? 

# 3**.~1** 

# 41.. "1 

# .4f)i liz (;'

## ~f 

# '1"1- 

# I 

# .tt) til. 7 f)**q~** 

### (

### ~If 

# )**"'~** 

# Ii 

# 13 

# "l u r 

# If;)**t:f~** 

## {(



# . Ii.)**'f~** 

## n: r'i6**~6**

Use 

### Bwsand MW data from previous Run? Yes No 

# _. Port Point**~p** 

### ("H2O) 

### Ts 

### ('1-) II Iv 

# IJ I 

# (, 

# Fit 1.. 

# ,. 'il Ifl ) 

# •Ci6 tt1.. tit**~2.. ~J..**  

# 6**,t;~** 

# Ut. (" 

# ,12 PI:l. 1 

# ,l'2.. 

# IJI-:J Iff) 

# 43

,. q- 1**~J** 

## f-4 

# 11 

# JfJ t1 

# ,1 t;J 

# iPI IlJ 

# 7' II.)

Time 

# v; (fe) Meter Meter Imp. Out llH In (oF) Out (OF) (oF) ("H2O)

### 87~fI 

## t;f1 

# 1., t Ii'}**",~** 

# //



# ...

# , 1- 7"1fi 

# 'or C(" -v

# J 

# ,**~I(;** 

# ul '-17 

# d 

# \// /6/6'**e..t~** 

# 4" 

# v/ r**~fI** 

### Ll' u) If '6(1) 

## c.f? 

# "f'b l)l**r~/.** 

### )-12- 

## fA1 t(}6 

# I Imp# 

# I Initial 

# I Final 

# I Net 

# I 1**71'~.** 

# t 

# ",/, ( 

## 2**.,~S-~,**

### ~'L 

## 3 

# u». I (/lg 4 

## f.P#',) , 7_"i' Total Train

Pre-Test Leak Check: 

# 12

# 15 

### Post Test Leak Check:

# c::J~)...

Form 1012 

### Fail CFM at 

# _It-L....-_ "Hg 

# :145 GE Energy

## Methods 2, 3 & 4 Field Data Sheet 

# 3 Run Number: Page

# L of 

# L. Date: Pbar ("Hg): Pstatic ("H20): 

## r, 71" Pitot ID: Pitot Cp: Meter ID: Meter Y: Meter t1H@i: Operators:

## ~'71 '**5V~1..{** 

### Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: Fail Post Test Pitot Leak Check: Fail

Time Port Point t1P ("H2O) 

### Ts (OF) 

# ")0 A- 

# , ,/1 t/[f"


# , 

# .**")~ ~,**  

## 'J**l~/I**

## ~6 

# ('1 '1 

# M('" 

# c**,~** 

# '3 

# qo r ,q 1

## 1~ 

# , .tiD**~~** 

## .'(0 

# 45 1**,~,** 

# 1/5' rl 

# , q?. 

# 1:1'''' (f

### .~ () 

# 'Ie /'-**,1~** 

# If:> Time Port Point t1P ("H2O) 

### Ts 

# po) {J ( t 

## 71

## /1~ '1.



## .**q~** 

## 4)" 

# J Jil**~j** 

### c.f 

## .1if2 

# f6 , 'fJ**~o** 

# /**,~** 

## :1**~5** I 

# .«'} 

# .qr



# .

# ,( Ii$' 

# i**.~** 

## I '1tr Gt 

# ,'il I.t" 

## 11**~I** 

### If") 

# , O'1Ul 

# n: ,iSS li'J

Use 

### Bwsand MW data from previous Run? Yes No

Time 

# v: (ft") Meter Meter Imp, Out**~H** 

### In (OF) Out (OF) (OF) ("H2O) 

# IS )

..**"l[.~7** 

# 7 

# 4q, f.t(



## 4)6" 

# lt4 'If s-o tII6 

# 'ff**t"'~ Cj~**  

### &(,1

### ¢~

### 4~ 

# a .61'""**Q~** 

# a ,400 

# I ( tr,1ft; 

# t« :(1 Imp# Initial Final Net 

## 1**~"'J,** "- 

### )'j(./ 

### /((.ll 

## 2**I~** 

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

### '1. 

### '") 4· 

## l. 

## 3 

# t"(1.0 I(t. 4 

# 407.'i1 caG4..fr Total Train

Pre-Test Leak Check: 9ss) Fail Post Test Leak Check: 

# YII/ CFM at "Hg

Form 1012 

# ::i46 GE Energy.9Jl' 

# I Project#: Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

## Methods 2, 3 & 4 Field Data Sheet
Pitot ID: Pitot Cp: Meter ID: MeterY: Meter LlH@i: Operators: Run Number: Page 

# -----L of 

## I Date: - 

# 1 1 

# 107 Pbar ("Hg): ....:..:?.f/n:....r.:.,.;:b...:-l

_ 

### Pstatic ("H20): 

# -,«: --'---"L.--

_



### Pre-Test Pitot Leak Check: 

### Fail

Time


# o7 )1; Port 

## A 

# A A A A A A A A A A 

# A Point 

## 1 

# 2 3 

# 4 5 6 

## 7 8 

# 9 10 11 

# 12 

# '1'(, 9(;



# 9 I Time Port 

## 8 8 8 8 8 8 

# 8 '8 

## 8 8 8 8 Point 

# 1 2 

## 3 

# 4 5 6 

## 7 8 

# 9 10 11 12 

# ,.8J--

.-76 1<\

t 

### Use Bwsand MW data from previous Run? Yes No

Time 

# v: (fe) Meter Meter Imp. Out llH In (oF) Out (oF) (OF) ("H2O)



# " JLI,

# '* '\Ot 

# 1./4 lfc..**.~~** 

### )- '"-(

< (}( 

# 'JIJ 

# -«: 

# y>**~)** 

### \ 

## 1-mJtt-I)-<.n i.J..(**'t~** 

# 1,

'-4"'" 

# <.;, 1\ 11**~')** 

### l..t 1--- 

# 1\ "i 

# ue ({'(,., 

# -;, 

# '17,,).4 i::o 

# I..{r 

# -;, (/ \ 1()1J \.

### \V 

### Imp# Initial Final Net 

## 1 

## 7qq.3 

# 770,:' 2 

# 75'1-7 '7i)C 3**fo3~.lo** 

# t:3' R 4 1(P'f3.'5**(,q~~** 

# 8 Total Train 

# 1'37,'1 ,**)..~~b~** f<)'


### Bws:



# ---

% CO2:

# 16'~-

% O2: 

### "1{)pl>



### Pre-Test Leak Check: 

### Fail Post Test Leak Check: CFM at "Hg

---- ---
Form 1012 

# :l47 

# ". GE Energy

## Methods 2, 3 

# &4 Field Data Sheet

J-O,? 

# )'! I/o'7 Jt1, 

### {t 

### Run Number: Page 

# _l of_ 

# t Date: Pbar ("Hg): Pstatic ("H20): 

# }, o IJ) 

### Pitot ID: Pitot Cp: Meter ID: MeterY: Meter LiH@i: Operators: 

## 4"1),/ Project 

## #: Company: Plant: Source ID: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: Fail 

# I Time 

# I Port 

# I Point 

# I LiP ("H20) 

# I Ts (OF) 

# I**c.01)~** 

## A 

# 1 

# .re CJ)..-··**~~** 

# J{ A 

# 2**.'7~** 

# 1JA 

# 3 .1-7'1 

# qy.- A 

# 4 

# .vc**q~** 

## A 

# 5 

# ..**e·~** 

# c'1 A 

# 6 vrt5 

# "7 OJ-- A 

# 7 

# "1«'**~')-** 

## A 

## 8 '< 

# '17 

# '1y A 

# 9 

# c,tf 9:>- " 1 

## A 

# 10 

# ..,'"1\ 

# '1)-

. A 

# , 11 

# <=tIl 

# tB'1

" 

## A 

# 12 "I:, -: 

# f5G. 

# I Time 

# I**o~** 

## Ij Port 

## B B B B B B B B 

# B B B B 

# I Point 

# I 1:.

3 4 

# 5 6 

# 7 8 9 

# 10 11 12 

# .-..73

Use Bwsand MW data from previous Run? Yes No

Time 

# v; (fe) Meter Meter Imp. Out llH In (OF) Out tF) tF) ("H20)

### i'~ 

# L?'7.L/47 1..If.,t; 

# L/L 78

..... ". 

# Y7 'lll!**"1~** 

# , 

# LIt> 

# LI 

# - ) 

# Lie... 1../( .-';

### ~O 

# (. G**~~** 

# '\J7**~)-** 

# (; '7,1 

# dtI5!J**I~[),)"il/** 

## ('") lj**!~** 

# 1t

-':-"1 

## #


## 2 3 4 Total Train


### Bws:



# ---

Pre-Test Leak Check: 

# @ Fail Post Test Leak Check: CFM at "Hg

Form 1012 GE Energy

### Project #: Company: Plant: Source 

## 10: Load: Stack Dim: Stack Area: 

## Methods 2, 3 & 4 Field Data Sheet 

# t1 )JilJC'

# ~11 (-6 L Pitot 

## 10: 00

# f3 

# A 4,' h**~Q1J,&** 

### Pitot cp:

# '#Jj,h-'~J/M1V Meter 

## 10: 

# 5

# v 0 

# hr Meter Y: 

# >']A; 

# I Meter ilH@i: 

# y: 71 I 

### Operators: Run Number: Page _,_ of 

# L. Date: Pbar ("Hg): Pstatic ("H20): 

# [flor

" C(

Pre-Test Pitot Leak Check: 

### Fail

Time Port Point ilP ("H2O) 

### Ts (oF) 

## B 

# 1 

# ,70 

# CIt' B 2 

# EJe;- 9\' B 3**i?{j~** 

# 1\ B 

# 4**~?-7** 

# 9\ B 

# 5 

# ,,910 

# 0;<' B 

# 6**~8q**

# I~ B 

# 7 

# .s«: ««: B 

# 8**~B()'** 

# 9(' B 

# 9 

# ,.·81 )\,- 

## B 

# 10

.**~!** 

# 7'\ B 

# 11 

# ,,7 '7 9\-'-- B 

# 12 

# L.'J 

# 9r

t.-

.... f76U1J",

. . J 

# if>**±.~** 

## '71")



# .. vt5? ('-Vi I 

### Time Port Point ilP ("H2O) 

### Ts (oF) 

## A 

# 1**~7~** 

# orLf -Ci: 

# 7/J A 

# 2**c~··)** 

# Cj'-f**ty~tvS'./\** 

## A 3 

# gg4 CfQ A 

# 4**~9}--** 

# 'l L ( 

## A 

# 5 r-rt57 CJr..·( A 

# 6 n

# Be;- qer A 

# 7 

# "lC qL( A 

# 8**.~l(** 

# Cjl.( A 

# 9


# ..9:\ 1 Li A 

# 10 

# .9'0 '1 L( A 

# 11**~q)-**

## ~'5

, 

### . 

## A 

# 12 ( :

### ~I

Use 

### Bws and MW data from previous Run? Yes No

Time 

# v: (ft;l) Meter Meter Imp. Out llH In (oF) Out tF) (oF) ("H2O) 

### }0).'>

### tto,,:L~c;

# ~" '-Ill 3\ ,)... \"



## •**lo~**

## -Z~



## . 01""\**~·c** 

# ( /CT'6 

# ,c' loy?:**~r** 

## • /0 Lj 

# 16 \i 

# i('-

iQG**~gJS-G,f,?,** 

# r;-o 

# LIe.**)~** 

# '\b



# ,

Pre-Test Leak Check: 

# .:& Fail Post Test Leak Check: CFM at ) jI 

### "Hg Imp# Initial Final Net 

### 1 

# 7W.7 7)--2._\ 2 

# 7(,/. / 

# 715c.h 'f 3 

## hkJ.

# e, f...'-fl-L. ( 4 

## 71t(.3**7/t::~** Total Train 

# ;;..t"n.<t 

# 2.s"',8

Bws:



# ---



# 1.49
Form 1012 GE Energy

## Methods 2,3 & 

## 4 Field Data Sheet Project #: Company: Plant: Source ID: Load: Stack Dim: StackArea: 

# 1. ]c r 

### Pitot ID: Pitot Cp: Meter ID: MeterY: Meter**~H@i:** 

### Operators: Run Number: 

# -:!f I Page 

# t of 

# I Date: - - 

# ')/I/D7 Pbar (UHg): ---=Z::....Lq,,--,-' (-'-./

_ 

### Pstatic(UH20): 

### _--"'-

..

## S=.L-

__

Pre-Test Pitot Leak Check:

# e~ Fail

Bws:



# --- Imp# Initial Final Net 

## 1**7S5~rs** ';77 '''' 

# 8710

..

# 7 2 

# 1775.0 

# 683

..9 3 

## S/Q,!-J**5/q~** 

# b 4 

# 7SQ,i-f 

# 7b2.2 Total Train 

## 280Q

..3 

## 2B'12.b 

# I Time 

# I Port 

# I Point 

# I**~p** 

### ("H2O) 

# I Ts (OF) 

# I B 

# 1 

# abC /0 I B 2 

# b7> /01 B 

## 3**r~** 

# /Y' /0')---- B 

# 4 .o

# ·70 /03 B 

# 5 

# bt'C, Joe, B 

# 6 "7L ' 

# La

.... o 

## B 

# 7 

# /,,7

.....**/c~** 

## B 

# 8 

# 07_'1 /0 

## B 9**~/(** 

# 10 B 

# 10 

# 0'21 /-0**r~** 

## B 

# 11 ",-p7 

# /0/ 

# o:»- B 

# 12 bC,'f 

# 1-8-0 Ts 

## tF) 

# t

# o>
JOy

ID?-·· 

# ie?-'· }0).--

## 7_~ 

## , /:0 2


# 4 

# 1
3


# 5
7 6

9 

# 10 11 

# 12 Point


# A 

# A
A A
A 

# A
A A A A A A Port Time

Use Bwsand MW data from previous Run? Yes No

Time 

# v; (fr') Meter Meter Imp, Out .6H In (oF) Out (oF) (oF) ("H2O) 

# i/0? (/7**J3~qJ-,** 

# '

..fl 

# 1..l1

...**~~** 

# J..." 

# '/I\l 

# lfcg 

# Y7 ')e,

e 

## i'roo 

# 1.f7 

# 31 • f}'6 

# S- Sf 

# /.J'1 

# 3',

t»« C 

## 52 

# 47 L(o 

# »v: tt;? 

# 52- 

# 4fl. '--10 I'YI-o 

## 1707"05"3 

# 5'3 

# 4B L{

# o '\t7



### Pre-Test Leak Check:

# (P~ Fail -"ost Test Leak Check: CFM at 

# 10 'Vl UHg 

# 1.50**~m** 

### 1012 GE Energy

## Methods 2, 3 & 4 Field Data Sheet
Run Number: 

# 'fr2 

# IUPage 

# .L of 

## _I

. Date:· 

# S--I

- D 

# 7 Pbar ("Hg): .2 f. [ 

## j Pstatic ("H2

## 0 ): <. 

# l' _---.-::.......-_- 

## • 71 

## y; 

# rcr-, r Pitot 10: Pitot Cp: Meter fD: MeterY: Meter LlH@i: Operators: o- 

### 71 " 

### Project #: Company: Plant: Source fD: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: 

## Fail

Time 

# 11- ()1 

# I Port 

## A A A A 

## A A A A A A A A 

# I Point 

# 1 2 

# 3 4 

# 5 6 7 8 9 

# 10 11 12 

# ..73 TstF) 

# lo:r 

# lc»- loy-

/0) 

## 10) 10) 

# Iv) Time Port Point LlP ("H2O) 

### Ts (OF) 

## B 

# 1

# ~'r 10;;1--

... 

## B 2


# .. S--. /0')-, B 

# 3 

# 4:"7 )0;-' 

## B 4

# ~G'**17;~** 

## B 

# 5 

# .»> /o>: 

## B 6 

# .i> tDY 

## B 

# 7 

# /;-7S- 

# i:u r: 

## B 8


# ...11' b--'Y B 9


# ...77**/C~** 

## B 

# 10**~7\** 

# I;; J

## B 

# 11



# ..74 [os-: 

# l,i (1 

## B 

# 12 

# ,,\C 't15

Use B

## wsand MW data from previous Run? Yes No

Time Meter 

## In tF) C)\ 

# 40**.~** 

# -7 Imp# Initial Final Net 

## 1 

# 8710" "7 

# eo«.« 2 

# 083

..9 {f.,l./.I 3 

# 5/g"b 51-V, 

### 4**7~2,2** 

## 7{),1 Total Train


## Bws:



# ---

y



### Pre-Test Leak Check: Post Test Leak Check:

Form 1012 

## Fail CFM at "Hg

--- 

# 151. GE Energy

## Methods 2, 3 & 4 Field Data Sheet**s~** 

# -I ,-? 

## 7 

# 21.6 1 

### Run Number: Page 

# .i.: of 

# L Date: Pbar ("Hg): Pstatic ("H20): 

### I, )

## ~~ 

# 1 Pitot ID: Pitot Cp: Meter ID: Meter Y: Meter**~H@i:** 

### Operators: Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: Fail 

# I Time 

# I Port 

# I Point 

# I**~p** ("H20) 

# I Ts (oF) 

# I**I~;** 

# 0 1

# 7 A 

# 1 

# n77 I,()Y 

## A 

# 2



# .. ,in [iJ)- 

## A 

# 3 II) 

# 'fu fur A 

# 4 D 

# i lo'r: A 

# 5 j 

# I loYA 

# 6**.~** 

## 0 

# le »: A 

## 7 

# rt«**t(D~** 

## A 

## 8 

# D74**JQ~** A 

# 9 

# flO 

# lol-/ A 

# 10 

# ,,'r 103 A 

# 11 

# .73 j 

# 0'3 A 

# 12**~70** )00 Time Port Point**~p** 

### ("H2O) 

### Ts (oF) 

## B 

# 1 

# •t/ Ity1 B 2 

# oC-, JoJ

## B 

# 3 " C.-7 

# /03 B 4**t'7~** /0) 

## B 

# 5



# ..**~9** 

## /03 

## B 6 1)70 

# /1}5 B 7 

# "7'-1 lob( 

## B 8

# ,~7B /0'-( 

## B 

# 9 

# 77**Jo~** 

## B 

# 10 p"7(.p !(}"l. 

## B 

# 11



# ..78 J(!)rO 

# 13Jf B 

# 12 

# ,&7 

# <i11

Use 

### Bwsand MW data from previous Run? Yes No



## r Time 

# v; (ff) Meter Meter Imp. Out**~H** 

### In (oF) Out (OF) (OF) ("H2O) 

# 7s '10

# l

# t.E.c-**~3 ~~**  

# If?-- 1 "

## ~1, )1, 

# 40 S

# "4- 'J,q 

## (1) 

## c;-'li 

# 37 

# 5s.. -V'**'~'/** 

# " ,15**~--r--** 

## '?> 0 '

## ,q~.4'A )1 

# 1ft:)**I~ '~**  

### Imp# Initial Final N 

## 1 

## qOJ-;tI 

## t1h I 2 £1JI1-( 

# {64.4 3 '))/),0 

## "{)..I, ,) 

## 4 7/J, 

## '1 7 {7.f> 

### Total Train
Bws:



# ---

Pre-Test Leak Check: Post Test Leak Check: f Oi}(j 

### Fail CFM at _---'-"-_ "Hg 

# 1.52

Form 1012 GE Energy

## Methods 2, 3 

# &4. Field Data Sheet Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

## '1,7/ / Pitot ID: Pitot Cp: Meter ID: Meter

## Y: Meter**~H@i:** 

### Operators: Run Number: Page _ of_ Date: Pbar ("Hg): Pstatic ("H20): 

# -=r-- 

# I r;*

-**f7'"~** 

# ')! 1/ 0-( 2-1, 

# Gl

Pre-Test Pitot Leak Check: 

# @ Fail 

# I Time 

# I Port 

# I Point 

# I**~p** ("H20) 

# I Ts (oF) 

# I A 

# 1**~-S-~** /I( 

## lu/ ')0 

## A 

# 2 to

# 7a> 117 A 

## 3 

# .s. J

# I,
A 

# 4. 

# ,..1':l( 

# J/7 A 

# 5 j>( 

# '0 1/7 A 

# 6 "c

# n Jl7 A 

# 7**/~q\** 

# III A 

# 8 

# .0157 )17 A 

# 9 

# _7Cf Jll A 

# 10



# ..7(, 1/

# 7 A 

# 11**I>tp~** 

# lit A 

# 12



# ..0 )/('

Use 

### Bwsand MW data from previous Run? Yes No " Time Port Point**~p** 

### ("H2O) 

### Ts (oF) 

## B 

# 1 v

## ~I 

# //7 B 2 

# ..**~~** 

# if7 B 

# 3 

# .rt /)In B 

# 4. 

# u71 lie, B 

# 5 

# ;..Rr /1& B 

# 6 

# ,;6!>r 

# .rt B 

# 7 

# ,,' 7 III 

## B 

# 8**.~** ?-- 

## 1/7 

## B 

# 9 

# A:>).-- 

# 17/ B 

# 10 

# ,73 /17 B 

# 11 

# It) /If 

# +0(0' B 

# 12**~'>~** 

# //'1 II-( l.{;fJ



### Time 

## V m 

### (ff) Meter Meter Imp. Out**~H** 

### In (oF) Out (OF) (oF) ("H2O) 

## JC:>-fl, 

# rn**--q~** 

# (J1JCf**~r** 

# t-t- '\7 

# A '/Cs"\ 

# 5"8**~G,**

## ~Lf J



## .**iC~~** 

# '1**~(**



### 1"\'1'7**&,~**

### ~7 

# 4<1. jr-fp' I

## &~ 

## '\'1 

# Y'I J\\, 

# V t'-( 

# Y'1**i~03** 

## !,1gI.Yt;G,**h~** 

# )<8 

# '{'\

'tV 

### Imp# Initial Final Net 

## 1 

# 0135

.. 

# 1**~7P.,o** 

### 2 

# 08Lf.cr 'q 

## IC;#-- 3 

# 520.3 

# s 8;)."**<~** 

## 4 

# 767.0 7G**'i",~~** 

### Total Train**J-Ifcn~'\** 

## :1

## 'ttl ". '.(
Bws:



# ---

Pre-Test Leak Check: Post Test Leak Check:

Form 1012 

### Fail CFM at 

## _-=---_ "Hg 

# 1.53 GE Energy

## Methods 2, 3 

# &4 Field Data Sheet Project #: Company: Plant: Source 10: Load: Stack Dim: Stack Area: 

### ],7 ( / Pitot 10: Pitot Cp: Meter JD: MeterY: Meter dH@i: Operators: 

## I,**7f~** 

### Run Number: Page 

# .L: of ( Date: Pbar (UHg): Pstatic ("H2

## 0 ): 

# 1B I)

# t/H!'z "/J-/67 24.1'('

Pre-Test Pitot Leak Check: 

## Fail

Time Port Point dP ("H2O) 

### Ts (oF) 

# .o.::J-JI A 

# 1**,,~** 

## Il<-f

, /I 

## A 

# 2 /70 

# }/<-{ A 

## 3 ()/ 

# II

# Lf A 

# 4 "jtt 

# JIY A 

# 5 

# .d!Sr;-- II'-( A 6 

# "q).-- 

# )fll A 

# 7**~g~** 

# )t'-f A 

# 8**,,~4** 

# llL( A 

# 9 

# 4>J1 I

# I<..f 

## A 

# 10 

# "7 "!> If

# L.( A 

# 11 

# G'"**'J~** A 

# 12 1 

# S-8 )10

;...


### Use Bws

### and MW data from previous Run? Yes 

### No

Time 

# v« (fr') Meter Meter Imp, Out llH In (oF) Out (oF) (oF) ("H2O) 

### 070{ 

## '77fl.

# ,c,q 4./ '3Cf )... \{ 

## • OO7i)-- 

# 4q '17 "1', -'(')7/, 

# 50 '18 "l,("'"

, O-,Y>-- 

## 5/ 

# 4R**~(("**


## , 07)-7 

# 52 tier ;}"



## . IfJ'I'\)- 

# " 53 

# yet**1~**



## h7)7 

# BOI.,471 

# 54 4'1 '\('


# \l7 Time Port Point dP ("H2O) 

### Ts tF) 

## B 

# 1



# ..**~7** 

# /F1 B 2

## ~~q' 

# JI'\ B 3**~l)--**

## 1J~ 

## B 

# 4 

# .ec II

# J-- B 

# 5 

# .es: 113 B 6 

# &-<:t4 IIJ---- B 

# 7 

# ,,(Ie Ito B 

# 8

# ~e~ 

# /II B 9

## p~ 

# II ').-' B 

# 10 

# .:7f.:5

# L/~ B 

# 11 

# ,71 

# ill B 

# 12 ,(PO Joe f7tlO

Imp# Initial " Final Net 

## 1 7;;'/· ( 

# 701./

.. i..f 2 

## (,9).

# « bqS

.. 

# &> 3 

## b:AI,O C;;2}", 

# 5 4 

## 7/t;.& 

# 7/6GCJ Total Train 

## ).**7C;~;** 

## I 7718. (;
Bws:



# ---

Pre-Test Leak Check: Post Test Leak Check: 

# 1''' 0 

### 0

Form 1012 

## Fail f"1 

### CFM at -, 

# In "Hg 

# 154 GE Energy

## Methods 

# 2, 3 &4 Field,Data Sheet Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

## S"VOL Pitot ID: Pitot Cp: Meter ID: MeterY: Meter LlH@i: Operators: Run Number: Page 

# .-L of _(_ Date: Pbar ("Hg): Pstatic ("H20):

## I~ 

# /).-/0] lA.?1**-.~**

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point LlP ("H2O) 

### Ts (OF) 

## A 

# 1**4~e** 

# 114 iU A 

# 2 

# .o: U'-/ A 

# 3 6' /)- 

# 111.1 A 4 

# .71 Ii

# t-/ A 

# 5 

# .s"7 

# 114 A 

# 6 

# ,c1t II'- A 

## 7


# . q /ty A 8 

# •

# ~tJ 

# II L1 

## A 

# 9 ( 

# t I I

# '-t ,. A 

# 10 

# ."li IlL{ A 

# 11 

# .o: J 

## iJl,.-- 

## A 

# 12 

# S""\" H.B

Use 

### Bwsand MW data from previous Run? Yes No Time Port Point LlP ("H2O) 

### Ts (OF) 

## 8 

# 1



# ..'-I ,I'i 8 2 

# ,70 11'1 8 

# 3 

# /.7 ( IlL{ 8 4**MP1'~** 

# ilL( ... 8 

# 5 

# .e»- f/L( 

## 8 '6

# ~8t;" 

# I/y 8 

## 7 ",CZO 

# /ILl 8 8

## #~15q Ill.{ 

## 8 9**;,f5~** 

## /IL.( 

## ,8 

# 10



# ..B)'- ilL{

8 

# 11 .,70 

# 1/ I AQ..:1..:::::I 

## 8 

# 12 

# ,s-3 J r:J

# f6 <t:;T J , 

## 7:' )

Time 

# v; (f1")



# 52 52 

# 54
5S 

# 46 If8 1-/'1 

# qq 56 J Imp# Initial Final Net 

## 1**75Y~~** 

## 7q " '-f 2 

# 73b.,O 

# 73'.5" 3**"/~** 

# ..':>**)/~,**

# , 4 

# 7''f,f) 77t'L Total Train 

# ;1.778,.')
Bws:



# ---



# 7 iff "Hg 

# 155
Form 1012 GE Energy

## Methods 2, 3 

# &4 Field Data Sheet



# 5.......... 

# -, Run Number: 

# -----lli<--

_ Page 

# _l of 

# _J_ Date: Pbar ("Hg): Pstatic ("H2

### 0 ): ft;3



# t. ") I 

### Pitot 10: Pitot Cp: Meter 10: MeterY: Meter**~H@i:** 

### Operators: {, 71 ,; 

### Project 

### #: Company: Plant: Source 10: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: 

### Pass Fail

I Time Port Point**~p** 

### ("H2O) 

### Ts (oF)



# 1:'f{ A 

# 1 

# .i: I

# rJ{ A 

# 2 

# ,e, (fJ 

# 7 A 

## 3 ,67**I~** 

## 7 

## A 

# 4 

# ; C7 

# ItJ 

# 7 A 

# 5 

# .{7 (07 

## A 

# 6 

# ,f) 11/ 

# 1 A 

# 7 , )&1 

# .,II

# 7 A 

# 8 ' 7S- /0 ] A 

## 9 

# • 71

.. J()

## 7 A 

# 10 ; 77 

# /07 A 

# 11 .(7 I 

# b5 A 

# 12 

# .(4 ,1-.'3 Time Port Point**~p** 

### ("H2O) 

### Ts (oF) 

# B 

# 1 ,(3 

# /()b B 2 

## 6)**I~G** 

# B 3 

# ,(, /07 B 

# 4 

# .C7 /07 B 

# 5 

# .tf 107 B 

# 6 

# .t» to7 B 

# 7 

# .7J /07 B 

# 8 

# .67 107 B 

# 9 , (C 

# 1°7 B 

# 10 

# .a: 16'6 B 

# 11 ,td 

# 1 6 ( 

# 4:oJ B 

# 12 

# .'/7 /oJ

Net

Bws:



# --- 1 2 

## 3 

## 4 1m #

Total Train Use 

### Bwsand MW data from previous Run? Yes No

Time 

## V m**(ft~)** 

### Meter Meter Imp. Out l!.H In (oF) Out (oF) (oF) ("H2O)

### Og~co 

# 8;)J 

# .,6,0... ,I ((J 

## 'J, '""-


# •otB«)) r.c(}- 

# r0 t,7

. ()**~B** 

# c"**~\ lj~** 



# ./)'" 'r),1 

# (\-\ 

# n l. 

# .z,

0'**'O~** 

# cC ,t;7- 

# LI 

# z,**A;r(~** "ell'" 

## ')l,P 

# «»>**L.f~**

## Dql~ 

# RLlf3.71Q t:"i <;''',**Lf~** '\. 

# I
OfoC02:



# 156 Pass Pre-Test Leak Check: 

### Fail Post Test Leak Check: CFM at "Hg

Form 1012 GE Energy

## Methods 2, 3 & 

## 4 Field Data Sheet

.. 

### Run Number: Page 

# --L of 

# .L. Date: 

# t.(/J /0'1 Pbar ("Hg): 

# ';1,\.1 'I :;;;- 

### Pstatic ("H2

## 0 ): _---:d.:..:-( 'L-5

_ 

## 1,7/i Pitot ID: Pitot Cp: Meter ID: Meter Y: Meter LlH@i: Operators: Project

## #: Company: Plant: Source ID: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: 

## Pass Fail

Time Port Point LlP ("H2O) 

### Ts 

## (OF) 

# l>-oc; A 

# 1**~(po**

# I~~ A 

# 2 i 

# Go**Jo~** 

## A 

# 3 "**.~** 

# lOr A 

## 4 

# .e«:**I~I** 

## A 

# 5 o 

# 6 '} I;)

# r A 6 

# c/O lnll A 

## 7 

# (**G~** 101 A 

## 8 p

## (.,~ 

# jo, A 

# 9 

# ct') /DI A 

# 10 r'

# c

# < JO, A 

# 11 prot) 

# t

# o 

# «: 'A 

# 12 "**i),.~** 

# Jo ]

, , i 

# I Time 

# I Port 

# I Point 

# I LlP ("H2O) 

# I Ts 

## (OF) 

# I B 

# 1 

# .:>ra¥ /0(., 

## B 2 

# .cc Jo" B 

# 3**,,/,~** 

# /07 B 4 

# .7( IOf 

## B 

# 5 

# 4'"q )() 

### { 

## B 6 

# pCl )0, 

## B 7 J.7 

# 7 J- /07 B 8 I?

# 7f /0-7 B 

# 9 

# ,77 

# /06 B 

# 10**~7y** 

# lin B 

# 11 o

# I J- 

## lot B 

# 12 

# ,,1 JOY I 

## ').--l'1

Use 

### Bwsand 

### MW data from previous Run? Yes 

### No

Bws:



# --- Time 

## Vm,(ft") Meter Meter Imp. Out flH In (oF) Out (oF) tF) ("H2O) 

## \)-oL\ 

# £b'\"

.. t; 

# Il 

# "i )"Lj t)?- ).. 

## -' 1).0

# 9 55"' 5

# tr '\'1 i

## 1.\

## L.i 

# 5"5 

# 54 Lf6t , 1)-

### J~ 

# 57 

# 55 '-{g

•**l~}-~(** 

# S8 55 4 (t)**I}-~ "'\~**  

# %Sq**~'iro**

## Lf~



## I

# >--1,Y 8'18..577' 

# 59 57 

# If(P \'t-, 

# ¥ I



### Pre-Test Leak Check: Post Test Leak Check: (t 

## 00 ()

Form 1012 

## Fail CFM at 

# q

# i11 "Hg



# - 157
GE Energy

## Methods 2, 3 & 

## 4 Field Data Sheet Project 

## #: Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

# ('1 

# )-)-A

# o)LfG

.**J:+'l)()~ ~",,-I\f.e**  

## 5Vo"/5 Pitot ID: 

### (9,C)

# 13

# A Pitot Cp: Meter ID: MeterY: Meter LlH@i: Operators:**~)** 

# U**~. l~/.**  

### Run Number: - 

# t -:7' 

### Page 

# .L. of 

# L Date: 

# \/;--10'7 Pbar("Hg): (

----- 

### Pstatic ("H20): 

### - 

# s=C

Pre-Test Pitot Leak Check: 

# {j;:2, Fail

Time Port Point LlP ("H2O) 

### Ts (oF) 

## ()'Y-{ A 

# 1 

# JI, A 

# 2 

# '4 }(t 

## A 

# 3 

# .cc; 11/r'j A 

# 4 

# 4>"S--**}o~** 

## A 

# 5 

# ,,6<' forB A 6 

# .cc: 1'013 A 

## 7 

# :.7D 

# Lef. A 8 

# '9 [0

## fj A 

# 9 

# ;.'3 JOI A 

# 10 

# ,'L/ /·0'

.. A 

# 11**,i~** )03 

## A 

# 12 

# "t)"\**J~** 

# i 

# I Time 

# I Port 

# I Point 

# I LlP("H2O) 

# I Ts (F) 

# I B 

# 1 .') 

# to 7 

# "

. B 2 

## ,., y'**l:(.)~** 

# B 

# 3 

# PI'(.

. iCf1 B 

# 4 

# ,;'**.~** )()7 

# B 

# 5**~b'1** 

# u« B 6 

# .',if }It:; 

# B 7 .4"' 

# ?':- 

# //'i B 8 

# ;,>bY' 

# J/4 B 

# 9 

# ",,7> 

# u«' B 

# 10 

# ;, '5**II~**

" 

# B 

# 11 .,**~q)** 

# lIt /33'6 B 

# 12 

# le...o lor;;-

Use B

## wsand MW data from previous Run? Yes No



## ,. Time 

# v; (ft") Meter Meter Imp. Out .6H In (oF) Out (oF) (oF) ("H2O)**i~)3**

### fft9.o~**~~** 

# (8 

# <y J.Vf 

# 1),'6 

# 0"1 i)?-

, J "; 

# t'1D 

## cg <,0 

## 11 18**~~O r;~**  

# 4- 0 1

### '1,"-\1, 

# bE 58 

# 4 7, I 

### ')'i 

# 8

# "'~ l?/ 

# 58 'f**;"1~)** 

# 872, 2 

# l.f3 

# b2 bO 

# l\b

...... 

# Y/

Pre-Test Leak Check:

# ~) Fail .. Post Test Leak Check: CFM at 

# q I

## Vi • "Hg

Form 1012 

### Net

Bws:



# ---

% CO2:

# I 0, 6

% O2: . 

# :J-..o. (



# :158
GE Energy

## Methods 2, 3 

# &4 Field Data Sheet Project #: Company: Plant: Source 10: Load: Stack Dim: Stack Area: 

# 1,71 ' Pitot 10: Pitot Cp: Meter 10: MeterY: Meter ilH@i: Operators: 

## Od·S 

# J

I,?**1~** 

### Run Number: 

# ._'...:-.-1

_ Page of Date: - 

# 5 -2

# -07 Pbar ("Hg):**-,-2.(-2.-f~** 

## __ Pstatic ("H2

## 0 ): •**f)~r** _..L-

_



### Pre-Test Pitot Leak Check: 

### Pass Fail

Time Port Point ilP ("H2O) 

### Ts (oF) 

# /;6h B 

# 1**~5** 

# 5 /07 150b B 2 

# ,57 

# Db 150'-., B 

# 3 

# ,b Lj J

# 07 (5"07 B 

# 4 

# 168 107 /5"0"+1 B 

# 5 

# #7S- 101 

# /5"O€ B 6 

# ,,70 JOb 

# l5'"oB B 

# 7 

# ,,8 

# 3 I**D~ {~69**  

# B 

# 8 

# p8lf /tJ£..! 

# Is-oct B 9


# ... «s: /04" 

# /5"oq B 

# 10 

# Cf/ 

# /oL:j IS/O B 

# 11 

# .,q/ 

# IlJI:..f 

# tsro B 

# 12 JJ 

# g,/:' - 

# -,**_CJ.13,~,-:::::-...-** 

# . 

# . /02

[OZ 

# 102 102



# qq
/02 

# !D2... ( 

# 10'3

10 J

## ~50 

# . 

# ,7 ,So ,87**~"?**



### ... I ) 

# .8 2


# 4 3 

# 1



# 5 

# 6 7
9 

# 8

11 10
12 Point 

## A

A 

## A A 

## A

A A A 

## A A A 

## A Port



# L 

# f)7 Time



# '{59 

# ius«

, t;OD 

# /458

Use 

### Bwsand MW data from previous Run? Yes 

### No

Time 

# v: (fe) Meter Meter Imp. Out boH In (oF) Out (oF) (oF) ("H2O) 

# 143Jf 872,1.{17**~O** 

# hO 5b 

# :z 111 ILj

# 3Cf I 

# bO 

# bD 5lf 

# uJ'1'+ 

# t 0**~O** 

# ;1 

# II. 'J..j.( 

## !:)L 

# bD 50 f 

# /-**5~** J 

# 04- bl 

# !q 

# Il'15' 

# ,**~.,** 

# G '/ 

# Lq 

# 150

# 'I 8Cf5.,taBf> 

# ?3 hI 

# u8 'II' 

# I Imp# 

# I Initial 

# I Final 

# I Net 

# I 1 h-- 

### ]FI 

# ,Lf g22,,8 2**I/j(~** 

# 737.5 3 

## 17/**~(i** 

# 5/8,,7 4 

## 77).· 

## 7 

# 77308 Total Train
Bws:



# ---

Pre-Test Leak Check:

# (pa~ Post Test Leak Check: ,. 

### 002 Fail CFMat 

# £5 ;-'1 "Hg 

# :159

Form 1012 GE Energy

### Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

## Methods 2, 3 & 4 Field Data Sheet

# M22Ao3t.+~ PitotlD:

# iiJIf1rt-r:M~f1 ife

# ~:~:~ri 38758 

# S

# 'i0

# 2S Meter

## Y: 

# I. 0 

# 05 

# > 90% Meter

## ~H@i: 

# I , 

# 7.18 8"7/ OFt!

# e£ Operators: 

# L**W7~B** SCi

.. 

# SB 

# 'sf: 

# -Ft / Run Number: 

# Z Page 

# .L of 

# L Date: 

# 5-2- <.'

# 7 Pbar ("Hg): 

## "2

# q.. 90 Pstatic ("H20):

### _----=.~S=__

# __

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point**~p** 

### ("H2O) 

### Ts (OF) 

# etz. A 

# 1 

# ., 5'-1 IDI 

# u.tz- A 

# 2 

# "174 (0 L 

# 't? A 

# 3**~'70** 

# [0/

/') 

## A 

# 4 

# ,,7S: 

# to 2- 

# oiL A 

# 5



# ..74 /0 

# I**~:J** 

# J'1 A 

# 6 

# , ,S- /0 I J



# 10 L.f, A 

# 7 

# ,78 10 

# I f 

### 'rJ 

## -Lf 

## A 

# 8 

# ,,7B fOZ. 'j..-, 

# !J A 

# 9 J 

# 7 L 

# /02-

btl) A 

# 10**~7C** 

# to2-**'/~** 

## '£) A 

# 11**f'7~** 

# /02- JJbl**,~** 

## A 

# 12**Ah~** 

# qq

Use Bwsand 

### MW data 

### from previous Run? Yes No Time 

# Ib67

te. D ,60 

# 161/ fbl/ Port 

## 8 8 8 8 8 8 8 8 8 8 8 8 Point 

# 1 2 

## 3 

# 4 5 6 

# 7 

# 8 9 

# 10 11 

# 12 

# .42



# ....50



# ..68 102- {04 

# I {)2.. 

# /0/ (67 

# /0 I

(o 

# I ICJ 

# I 

# /o:z. to! 10 

# I

Time


# 155, 

# 51

55b 

# bt> hOI 

# bl 1.,0 

# 60 bO

bO 

# 54- 5{ 

# :2 

# In
I



# • Imp# Initial Final Net 

## 1**I;I«).~** 

# 83'-1.6 2

## ~q',J**bt:ttD,,~** 

## 3 

# ,;)..\


# .. f,22.Q 4**'7'~/'** 

# 7/8.5 Total Train**:l.~)(.,** 

# B

Bws:



# ---

Pre-Test Leak Check: 

# CPaij) Post Test Leak Check: 100 {

Form 1012 

### Fail 

# q" CFM at 

# /11 "Hg 

# =160 GE Energy

## Methods 2, 3 

# &4 Field Data Sheet

Run Number: 

# -If--.J Page 

# -L of 

# I Date: - 

# 1;;/3/07 Pbar ("Hg):**_1.-"~_.**

## 'l-r-()

_ Pstatic ("H20): 

# ---",;<--Ok"---_ Pitot ID: Pitot Cp: Meter ID: MeterY: Meter L\H@i: Operators: 

# 5VOt,Cf Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: 

# 8 Fail

Time Port Point L\P 

### ("H2O) 

### Ts (OF) 

# «uo A 

# 1 

# ,·GI /0'-/ A 

# 2 (61;, 

# IVI.I A 3 

# 1'1,1- 

# Ii) 'J 

# A 4 J

# 7' 10'--1' 

# A 5 k

## 7~ !C'i 

# A 6 

# ,--l ltJy A 7 It

# '.Ie; 104 

# A 

# 8 

# Ii·**'~**

### /{)~ 

# A 9 . f 

## J)-- 

# to3 A 

# 10 

# sf '1 

# i O'/" A 

# 11 

# flY lei A 

# 12

< 

## 1)'8 

# tfJ Time Port Point L\P 

### ("H2O) 

### Ts (OF) 

## B 

# 1 

# ..tb/ IcY B 2 

# ..A 

# 7 loL( B 

# 3 

# .:11 /Oi..{ B 

# 4 

# ,,83**IC~!** 

## B 

# 5 

# ,A ')-,**j.~y** 

## B 

# 6 

# , (

# ~3 tel..[ 

## B 

# 7 

# I**~,** 

# /oo B 

# 8 

# 1,/**~4f** 

## B 9 

# 1,/ ttex B 

# 10 

# IJI 

# 11 B 

# 11 

# ,qfj 

# q7 01,{? B 

# 12**JB~** '1)

Use 

### Bwsand MW data from previous Run? Yes No

Time 

# v; (ft") Meter Meter Imp. Out LiH

.. 

### In (OF) Out (OF) (OF) ("H2O) 

# n:"01 

# If).U/'l..

# 7**)~** 

## VI**.~** 

# A'" 

# rr 'Ir LIt 

# lJ'O -S'7 

# n- Jl Li3 i- 

## 0 

# -->?



# · o· yy 

## 1-**~5** 

# u 0 

# ') c

ol}-l 1.1 

## (p l 

## J**~~** 

## !()11y 

# < 42 

# 15" 10'1'3

# '1 qL/Z.3CJS 

# Ll1 

# Lf3**~5**



# ...h V Imp# Initial Final Net 

### 1 

# 790.,D 'f1;;.J...,

## J2 

# 758

..0**17~,9** 3 

# bs7

.. 5 C, 

## )7,,7 4 

## 6QLf..

# S 

# (Oc

# n-s- "

,. 

### Total Train**:L~HO** 

# .2.'1 i \**~3** Bws:



# ---

% CO2:



### Pre-Test Leak Check: 

# CJ
Post Test Leak Check: • 

### Fail CFM at 

# IB 

# i fl,,"Hg 

# 1.61

Form 1012 GE Energy

### Project #: Company: Plant: Source ID: Load: . Stack Dim: Stack Area: 

## Methods 2, 3 

# &4 Field Data Sheet

# ~t(¢**~:~~h- ~:~:~p**  /JOY!

# A !;:;:bb Meter ID: 

# tnss.

__ 2

..... -t;;l Meter Y: (.. 

## Ah? 

# S- 

# >'U'I. Meter

## ~H@i:**1.d<-/...Lj7/~~,--=-~_** , r 

# 1( I 

### Operators: "1'-v 

# U Run Number: 

# tfr= / Page 

# .L of 

# L Date: 

# TIJ/oZ Pbar ("Hg): _'

_ Pstatic ("H2

### 0 ): _-_,**~L--** _



### Pre-Test Pitot Leak Check: 

# (f;) Fail

Net 

# qi , q7 

# q(**~p** 

### ("H20)



## 3 

# 4 2



# 5 1

7 8 

# 6

9


# 11 10
12 Point



## B
B B B B B

B B
B B
B 

# 8 Port



# 1(7)-0) II Time Ts 

## tF)



# '1 In 

# :1'1 

# -n**,~ ~p**  

### ("H20)



## 3 

## 2


# 4 1

6 

# 7
9 

# 8 "5



# 10 11 12 Point



## A A 

## A
A 

## A



# A
A A

A A A

A Port Time

Use 

### Bwsand MW data from previous Run? Yes No 

# Iw{)'Y·

Time 

# v; (fe) Meter Meter Imp. Out .D.H In 

## (oF) Out 

## (oF) (OF) ("H2O) 

# o 82!.f. 9L/2

.. 875 

# '17 LIb ·45 2 

# if{, 082' 

# LiB 415 J./Lf .O83/" 

# 5 Lj

## ·lb 

# 1./3 

# b83 c 

# S3 L, 

### to 

# 4.3 084'


# . 

# .**~,c;** 

### l, 

## b**r..p~** 

# 08'1 0 

# '\JV**"'-"~** L
" 

# -/ lr\ 

# , 085l., 

# q,bl.//78"7 t)-t 

# ill LJ"\ Bws:**--~**


## % CO2:



### Pre-Test Leak Check:

# ~~~ Post Test Leak Check: •0**~'"** 

### Fail CFM at "Hg

--- 

# 162 Form 1012 GE Energy

r:' •.**-'"",.,.~** ••**-~:** 

# -

## Methods 2, 3 & 4 Field Data Sheet Project#: Company: Plant: Source 10: Load: Stack Dim: Stack Area: Pitot 10: Pitot Cp: Meter 10: MeterY: Meter ilH@i: Operators: 

# /.71f; '7'-0 

# U Run Number: 

# 3-. Page 

# -.L of 

## _/_----=...;:"'----- Date: 

# 5/3 

# /0 '7 Pbar ("Hg):

## ~'i 

## q --"'------',--- 

### Pstatic ("H20): 

# _-_L"-'5=--

__

Pre-Test Pitot Leak Check: 

### Fail

I 

## Time

.. 

### Port 

## A A A 

# A A A A A A A 

## A A Point 

# 1 2 3 4 

# 5 6 

## 7 8 

# 9 10 11 12 

# .•t;l; Jll{ 

# C17

(,t'l 

# q1 Time Port 

# B B 

# B B B B B B B B B B Point 

# 1 2 

# 3 4 

# 5 6 

## 7 8 

# 9 10 

# 11 12 

# CIa 

# I , f I , (J 

# 17 

# CZ7

c "7

Use B

## wsand MW data from previous Run? Yes No

Time Vm(fn Meter Meter Imp. Out llH In (oF) Out (oF) (oF) ("H2O) 

# DUg 

# IGteu g}Jo 

# '}3 )"/ 

# 1 :t It

## M4~ 

# 5S 51 

# 1.L.f**D~lf'8** 

# 50 51 L.j 

# r- (')q**.;;--~** 

# '>8 52 t... ,0



## . OCl l)f, 

# 60 

# 52 '-:,-1**I.DO~** 

# "17 b' Ii:; 

# ,'7

1100

# B 'Qe8"Z/3**~J** 

# 5Lj 

# ),

m \j



### Pre-Test Leak Check: 

# .Q:l Fail ,-:,- 

### Post Test Leak Check: CFM at 

## Q i

# t1 # 

### "Hg

Form 1012 

### Imp# Initial Final Net 

## 1**7)'~··~**

### 7~'3JO 

## 2**7?z~** 

# ...**3B~;;l.** 

## 3 I<)/q

... 

## I t 

## "ICJ;3 4 77(,r-**777.~** 

### :L Total Train


## Bws:



# ---

o. ') 2l)



# :163

GE Energy

### Project #: 

### Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

## Methods 2, 3 & 4 Field Data Sheet 

# ,11

# J-~ b1'f(, PitotiD 

# 008 

# A**I'k~** b= 

# 'R.e-:

...**l~** Pitot Cp: 

# rJ;:I,!.;\J Meter iD 

# 7**~r** MeterY:

_ Meter .1.H@i: ( 

## 1/ Operators: 

## ::rJc. I 

# it< Run Number: Page....L of 

# L Date: . 

# S-!J/07 I ; 

### Pbar (UHg): Pstatic ("H20): 

# ---,'=3£'----

..**-::'~;r**

.**:~;j'.**



# q8 q7



# ere

qz.. \.qp 3 IJ 

# 70 4 f 

# 73

7 , 

# S 

# Lf

10 

# .ec 11 

# ,73 12 

# 1140 B B B



## B B
B

B B B B B B Port Time Pre-Test Pitot Leak Check: Pass Fail

Time Port Point .1.P ("H2O) 

### Ts 

## (oF) 

# '1 t.f7 A 

# 1 

# I1b3 

# q8 A 

# 2**J~q** 

# q8 A 

# 3 

# .175" 

# qe A 

# 4 

# ,7Q 

# qB A 

# 5 

# J88 

# qg A 

## 6 

# 4Cf q8 A 

## 7 

# 8f 

# qe A 

# 8 

# [86 

# q8 A 

## 9 

# /61 

# qa A 

# 10 

# IBC! 

# q8 A 

# 11 

# /30 

# qe A 12 

# 1Gb qf;

Use Bwsand 

### MW data from previous Run? Yes No

Time Vm(fe) Meter Meter Imp, Out f1H In 

## (oF) Out 

## (OF) (oF) ("H2O) 

# 1052 

# IQAR II

# 5 06 

# 5b 

# 5S '-17 

# :z i". 

# D57 58 5S t.jq

102- :;>0 

# 55 

# 47 107 

# 5b 

# 41 f

# /IZ 

# r y**~&** 

# 41 f 

# 117 

# \I/ h 

# co Lil 

# 1/22 

# oif

.. 

# b3B 

# "I .-r;f/ 

# q7 \ 

# V Net

Bws:



# ---

Pre-Test Leak Check: Post Test Leak Check:**~OO** 

# /. Fail CFM at 

# /0 II). "Hg 

# 164
Form 1012 GE Energy

## Methods 2, 3 

# &4 Field Data Sheet Project#: Company: Plant: Source 10: Load: Stack 

### Dim: Stack 

### Area: 

# M)-}-A 

# (J><-{ 

# G Pitot 10:

# :lt~thbi~ 

# n.....\k. PitotCp 

# 'lo ".

. Meter 10: 

# Suo?--$ Meter

## Y:



# '4g;., Meter**~H@i:** 

# 'J 71 ' Operators: 

# [IV!J ( Run Number: Page ) of 

# I , Date: - - 

# t?/JI07 Pbar ("Hg): t -----,-=---- 

### Pstatic ("H2

### 0 ): - ..

# r

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point**~p** 

### ("H2O) 

### Ts 

## (oF) 

# J).J3 A 

# 1 

# .' 1'4 P)q



## (ff 

# 17) A 

# 2 • 

# '14:1 l'1 A 3 

# if, 

# 7 

# '1 A 

# 4 

# " 

# '& 

# q A 

# 5
, 

# 13 t. 1:::1 

# A 6 

# ,a & R. 

# .C1 A 

# 7 A

### V 

# q t.'1 A 

# 8 

# J I 

# 0 gO) A 9 

# t f 

# I**go~** 

# A 

# 10 , # ({) 

# t1

# (1 A 

# 11 !

# 9'7 

# &M A 

# 12**,7--:~ !I~** 



### Use Bwsand MW data 

### from previous Run? Yes No Ti

........... 

### Port Point**~p** 

### ("H2O) 

### Ts 

## (oF) 

## B 

# 1 

# "7'1 #? B 2 

# /1:J-- #t B 

# 3**Q~')** 

# t B 

# 4 

# otto**fJ~** 

## B 

# 5 

# .e $(. B 

# 6**~<:.** 

# J, 

# ?c: B 

# 7 

# eJlt;" [)'11 

## B 

# 8 

# /to 

# 81 B 9 

# /10 

# 84 B 

# 10 

# "QO 

# 6>'1 B 

# 11**fq~** 

# 89 J;r..l/n B 

# 12 plf"7 

# h'cr !tI

# l.tfJ)

Time 

# v: (f1") Meter Meter Imp, Out**~H** 

### In 

## (F) Out 

## (oF) (oF) ("H2O) 

# IJ22.0 012"OjL1- 

# bJ 

# 58 48 '2 'j"



# IZ25 

# '"' f SCI i.. 

# f '1230 b3 

# c:;q 

# ... 'J



# 1235 ;(/ /of) 

### L 

## /24D 

# 'l -, ,,0 U J 

# 11'245 \ 1/ t,& {pO 

# YI 

# /250**ID~f,'l1.** 

# q 

# b, W (.1' \ 

# 1/ Bws:



# --- Net

Pre-Test Leak Check: 

# Ci5iS'V Post Test Leak Check: .000

Form 1012 

### Fail 

# l' CFM at "Hg ---\----- 

# :165

• GE Energy

## Methods 2, 3 

# &4 Field Data Sheet

Pitot 10: Pitot Cp: Meter 10: Project #: Company: Plant: Source 10: Load: Stack Dim: Stack Area: 

# 't

... 1( I 

# }(J;1f'ib MeterY: 

# I, 

# 05 Meter

# ~H@i: 

# t"7

# l-l Operators: 

# TWZR Run Number: 

# ---.t..-:.d.1!>oc,---- Page 

# --..L. of _'

_ Date: 

# S/3/D7 Pbar ("Hg): 

## --=-i-=::f ::..::..f

Q

_ 

### Pstatic ("H20):

### "'_"'~S--!...-- 

# _

Pre-Test Pitot Leak Check: 

### Fail 

# q/

Of 

# I 

# ,R7 2


# 4 

# 1
3


# 5
7 

# 6

9 

# 10 11 

# 12 8 Point 

## B B



## B
B
B B
B
B


## B
B B Port



## , B

..... 

### ./ 

### Time Time Port Point**~p** 

### ("H2O) 

### Ts (oF) 

# 1,/1(r{ A 

# 1 

# ,,6 '10**rtf1J~)** A 

# 2**r~** 

# <::to

./ v 

## A 

# 3 

# (7 

# 010 ,)A A 

# 4 L 

# <ltU



# .. A 

# 5 o 

# '3 

# go A 

# 6 ,,(,

# n: '10 A 

# 7 ( 

# '3 qo 1: 

## A 

# 8 

# ,a 

# , t{J A 

## 9 AI' 

# 'J cIAJ 'A 

# 10 c 

# vt cI/O 

# . A 

# 11 'J

## ~y 

# t

# r(j A 

# 12 

# ct l 

# J3&;

Use 

### Bwsand MW data from previous Run? Yes No

Time 

# v; (ft;j) Meter Meter Imp. Out**~H** 

### In (oF) Out (oF) (oF) ("H2O) 

# 13l..flJ

# 035.BhY 

# h5 bl 

# LIb ::2 

# 1 \1\ 

# 13"4':>**~5 ~I** **Lf~** ''':; 

# 5D {;6 

# 62- L/-,Y

-;SC; 

# t7**{~-J-** 

# qy**~L,** 

## 00**fd~·** 

# 6":J.- 

# qy If.,[05 

# ," t.J..**'~f** 

# qy 

# IL [0

# 1~#""74 -t:,q**~3** 

# l-fr- \ 1/ 

# -tJ Imp# Initial Final Net 

## 1 

# 70Jl-f."

# Cf {fIr;:

# r 2 

# 73Q

..Y**7)/~** 

### L 

### 3 

# 5Jq

.. 90.( 4 

# 1718.,) 778.,

# 7 Total Train
Bws:



# ---

Pre-Test Leak Check: 

# (pass) Post Test Leak Check: f**e~** 

### Fail CFM at 

# -----'g "Hg

Form 1012 GE Energy

## Methods 2, 3 

# &4 Field Data Sheet



# --- ....c Run Number: Page 

# L of

# L Date: Pbar ("Hg): Pstatic ("H20): 

# roBA Pitot ID: Pitot Cp: Meter ID: MeterY: Meter**~H@i:** 

### Operators: 

# '0. ) I 7 

# >

IjP/,**JVU.l~** Project

### #: Company: Plant: Source ID: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point**~p** 

### ("H2O) 

### Ts tF) 

# t'-f(\ A 

# 1 I

## ~G C, 

### Yl

)

## ((~fl) 

## A 

# 2 

# 14 0 

# 1


# . A 

# 3 ...- 

# '1'3 { 

### ') 

## A 

# 4
, 

# I(p 

# l\.'J A 

# 5**.~** ?--' 

# 01.'1 A 

## 6 

# 3-**1.,r~**

, 

### . / 

## A 

# 7



# ...q/" 

# 4J A 

# 8**~q.1..#.** 

# tlj
',L 

## A 

# 9 u

## ~3 

# • A 

# 10 il

# e

. 

# 'lrr: ./ 

## '''i . 

## A 

# 11**~c** 

# l 'lP A 

# 12 

# .&0**~'1**

, 

# I Time 

# I Port 

# B B B B B B B 

# B B B 

# B B 

# I Point 

# I 1 2 

# 3 4 

# 5 6 

# 7 

# 8 9 

# 10 11 

# 12 Ts tF) 

# 91 eLf



# 'y

Use Bwsand 

### MW data from previous Run? Yes No

Time 

# v;**(ft~)** 

### Meter Meter Imp. Out t.H In (OF) Out tF) tF) ("H2O) 

### fJ, L '':;i

# ) OSq

..

# t 7b**~8** 

# 1oL..f 

# ss :2 

# 1;1**,~** 

### rt., 

### J'" 

# 4,8 05 55 'I.. C:;

.. 

# .q 

# ht:t 5'1 LJ 

# 5f: 

# 70 

# bS 

# 5Y 5.0 71 

# hb t;LI- 

# /508 -<;t7 

# 7/ 

# 66 

# 5Y**ISI~** 

# OB3

.. 

# Bh 70 bb 55

l

# V 1m 

## # 1 2 3 

## 4 Total Train
Bws:



# --- Net

Pre-Test Leak Check: Fail 

# q . Post Test Leak Check:

## I,"-,O~O=O CFM at 

# 111. "Hg

Form 1012 GE Energy

### Project #: 

### Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

## Methods 2, 3 

# &4 Field Data Sheet 

# MtL4.()3 

# 'it Pitot ID: 

# Hih

# b

# wCi_Iaco

# nAte Pitot

# ce.**Id(t/b.r~** Meter ID: 

## $YO

# b...5v 

### Meter Y: 

# )1"

# r.. Meter t1H@i:

## ~77-J~~- 

# ./4. 7 ( Operators: Run Number: Page 

## _f_ of 

# L Date: Pbar ("Hg): Pstatic ("H20): 

# ,

- ..66

Pre-Test Pitot Leak Check: 

### Pass Fail

Time 

# 1223**f'IIL~**



# /228 Ie II 1.-

# t¥ )

... Port 

## A A A A A A A A A A A A Point 

# 1 2 

# 3 4 

# 5 6 7 8 9 

# , 10 11 12 

# f (10 

# LOqq ffI' 1 

# q8
0'



# (.7 

# 87 Time



# 1

# r1 If



# 1/232 I] 

# l

# 3 L 

### Port 

## B B B 

## B B B B B B B B B Point 

# 1 2 

# 3 4 

# 5 6 7 8 9 

# 10 11 12 

# I?qb 

# ,CJB

(.dO



# ,93



# ..8b 

# 9b



# 97 

# 97 97 

# 87

Use Bwsand MW data from previous Run? Yes No

Time Meter In 

### tF) Imp. Out 

## L1H (OF) ("H

## 20) 

# 1//5"" 

# 9 

# 9**IJ/~r;.** 

# 00 Ii20 ') 

# c 2 

# BB qO q 

# h3 2 If\ 

# bZ 

# h2

bl 

# hI 61 \1 Bws:



# --- Net

Pre-Test Leak Check: 

### Fail / 

# f

.... Post Test Leak Check: ,,--,.0,---,0,,--,-'

__ 

### CFM at _ 

# f

# n "Hg

Form 1012 

# :168

GE Energy

### Pitot ID: 

# 008

# A Run Number: 

## J' 

# "2 Pitot Cp: Page 

# .L: of 

## L: MeterlD:

# e81$~3B758Date: 

# S-B-07 Meter Y:**I~** 

## 005 J:>bar ("Hg): Meter L\H@i: 

# 1,,"778 Pstatic ("H20): 

### Operators: 

# T-IN/ RB Methods 2, 3 & 4 Field Data Sheet Project #: 

# /122.

# A 6 

# 34;; Company: 

# =mt:bjil)qTacDni!e Plant: Source ID: 

# 3

# vo LIt Load: 

# 5re

# ate,..**+.--hQ-n---:Cf::-O----::~::--:i:).------** Stack Dim: StackArea:

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point 

### L\P ("H2O) 

### Ts 

## (OF) 

# 134 !.. 

## A 

# 1 

# .,85 (DO

, L'1\;1 

## A 

# 2 IpO 

# qq I' I 

## A 3 

# 1".0 

# qq A 

# 4 

# I" J 

# qCJ A 

# 5 

# f

.. J 

# qq A 6

# I~O 

# qq A 7 

# 110 

# qq A 

# e**I~O** 

# qq A 9 

# /,,0 C 

# c A 

# 10 

# 41q C,)C 

## A 

# 11 

# ,8t.., 

# qq**,~** 

## A 

# 12 

# ,,73 

# q"

Use B

## wsand MW data from previous Run? Yes No Time Port Point



### .L\P ("H2O) 

### Ts 

## (OF) 

## B 

# 1 LJ

# 9) 

# ID

# o B 2



# ..92 /00 B 3 

# ,qOj /00 B 

# 4**~O** 

# qq B 

# 5 

# I• J 

# 99 B 6 

# .) 

# q'1 B 

# 7**~D** 

# qq B 8 

# "qCj 

# c**~q** 

## B 9 

# 4>Cjb c 

# 8 B 

# 10 

# t>q3. 

# £1A B 

# 11



# ..85 q7**'35~** B 

# 12 

# A7q 

# 88 (**'t.r~)** /



### Time 

# v; (ft") Meter Meter Imp. Out 

## LlH In 

### (oF) Out 

### (oF) (oF) 

## ("H 2

### O) 

# 323 

# 29/{,,7'17 

# 94 9.5 b3 2 

# j" 

# '.328 °3 

# 95 S9

3":i'=S 

# (3 94**b~ ·3~R.**  

# '7'3 

# Cf3 

# 63 3lf3
I 

### £:; 

# 3 9'3 f:/O 

# 13L18 

# ,V 

# c'Lf 

# 43 

# S8 11353 

# SIC:,,2 

# JJ 5 

# q3 r:;q 

# \ I 1m 

## #


## 2 3 

## 4 Total Train


## Bws:



# --- Net

Pre-Test Leak Check: Post Test Leak Check: 

## ,,0

# 0 2

Form 1012 

### Fail CFM at 

# 8 (n, "Hg 

# 169 GE Energy

## Methods 2, 3 & 

## 4 Field Data Sheet
Project #: Company: Plant: Source 10: Load: Stack Dim: Stack Area: 

# B

# Ml;

# ~-&**~o~ftE** SIIO'Lt'j Pitot 10: 

# 008 

# A Pifot Cp: Meter 10: 

# :367 5 

# B MeterY: /" 

# 005 Meter

### ~H@i: 

# 1,7J8 Operators:

## TL~WL+--7--Lg~~=---_ 

# 7 Run Number: 

# ::J Page 

# ---L of

## l~-::zI---- Date: 

# 5-8

- 07 Pbar ("Hg): Pstatic ("H2

### 0 ):

Pre-Test Pitot Leak Check: 

# Pass Fail Post Test Pitot Leak Check: 

# Pass Fail



# 87 q 7

## ~q5



# I

.. 

# I 

# /

.. 1

/0

{



# f} 

# B

/2- 7 

# I Point 

# I
fA It' 

# f41'2

/4/') 

# I Time 

# I Port Time Port Point 

## LlP ("H2O) 

### Ts (OF) 

# 141(" 

# A (**,7~** 

# q7 V,

## ~f~) 

# 2 .,q

# R 

# q, I\.... 

# / "3 

# /

.. / 

# q7 L{ # 

# q7 .,7J.. 

# qf .,2 

# c 

# )t? 7 II 

## C. 

# '1 

# R 

# AO 

# c q 

# a "e

# '4: Qq (0 C! (

# r4 C 

# q 1/ 

# "As c

# ":fq 

# 11420 [2 

# 875 

# 92 vt I_c)) ../



### Use Bwsand 

### MW data from previous Run? Yes 

### No

Time 

## Vm 

### (ff') LlH 

### ("H20)


# 1/1. 

# /7 

# e« {l22 

# 'q It 

# 27**~q** 

# /t137 \1/ C.

# 0 " 

# B'7 SA


# SR 

# 60 2 j""



# \V Imp# Initial Final Net 

## 1**~I)I../.** 

## -11< 7 

## 2 

## 70C:,;7 

# 171l:"-"1 3

## 6~1."**~~** 

# ..q 4 

# 16

# HV

..f 

# Il.<:n

......., Total Train


## Bws:



# ---

Pre-Test Leak Check: (paSS) Post Test Leak Check: 

## ,,002 

# Fail CFM at 

# 8 

# t t\ i 

### "Hg 

# :170

## Methods 2, 3 & 4 Field Data Sheet Project#: Company: Plant: Source ID: Load: Stack Dim: Stack Area: Pitot ID:

### -"O=~...:....'...:.:.A

_ 

### Pitot Cp: Meter ID: 

# 6' 

# 8 

# 15 0 MeterY: 

# I,' 

# <r Meter

## ~H@i: 

# 1,7 

# I f3 Operators: 

# T 

# WI R

# g ( 

### Run Number: 

# J / Page 

# .L of 

# f Date: - 

### )',.7·

# tn Pbar ("Hg):**--=~~.** 

### {'-----

__ Pstatic ("H2

## 0 ): _---=()'--,,"--

__



### Pre-Test Pitot Leak Check: 

## Pass Fail 

# I Time 

# I Port 

# I Point 

# I**~p** ("H20)

# I Ts (oF) 

# I bRIO A 

# 1**~qO** 

# /02 

# 0 A 

# 2 

# ",8S- i02 

# ( 7 (6) A 

# 3 .C! 

# i 02 A 

# 4 I A 

# 0 

# io2 A 

# 5 ) # 

# f ID

# 2 A 6 

# I, 

# ? 102- A 

# 7 

# III /02- A 8 J

# .o /0"3 A 

## 9 

# t!qq 

# io2 A 

# 10 

# "qS' 103 A 11


# ..qo**16~** A 

# 12**~88** 

# q-:s Time Port Point**~p** 

### ("H2O) 

### Ts (oF) 

# B 

# 1



# ..88 /0 B 2 

# ,,87 102

" 

# B 

# 3 

# .es: J

# Z>2 B 

# 4 

# ',0 /DZ B 

# 5 

# j. () 

# 10"1 B 6 

# #0 

# /03 B 

# 7 .,0 

# /02- B 8**~O** 

# /02- B 9 

# 'Jqq 

# I

# oZB 

# 10 

# '/ ID2. B 

# 11 

# ,QZ ,"02- 

# 0820 B 

# 12 

# ,84 

# Cfl

(7

# ],oJ

Use 

## Bwsand MWdata 

## from previous Run? Yes No

Time Meter Out (oF) Imp. Out 

## .b.H (oF) ("H20) 

## N



## Bws:



# --- 2 3 1

4 1m 

## #

Total Train 

# SCf 2 

# in



# 57 58 

# 57 \V 58 

# 80

0633 

# '1' j 

## 1;2<0 • I 

# I 

# 0813 

# 78



# oB,38 2/Q, 

# qz

# '1 

# E3

Pre-Test Leak Check: Post Test Leak Check: 

## ,00 

# I Fail 

# 0 '" CFM at 

# --=-L I

# V\ "Hg

Form 1012 GE Energy

### Run Number: 

## -;f:. 

# ;<-. Page 

## f of 

## I Date: - - 

# 5-8- 0 

# 7 Pbar ("Hg): 

## _2--'-,0':",-6-:--

__ Pstatic ("H2

## 0 ): - 

## ti, 

# g Pitot ID: 

## 008 

# A Pitot Cp: Meter ID: 

# 88750 MeterY: 

# 1.1"(**Meter~H@i:** 

# r-B Operators: 

## T

# =Z R.f? '"6- 7 ( 

## Methods 2, 3 & 4 Field Data Sheet 

# M22A03Lfb 

# H;bh;nj Taco

# ",te

,., svo3D 9070 Project

### #: Company: Plant: Source ID: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: 

### Pass Fail

Time Port 

# A A A 

# A A A A A A A A A 1 

# ,,-rq 2

...

# 80 3 

# t,o
5 

# /,:J- . 6 

# I, 

# f

9 J

# (0 10 

# ,a8 11 I

## ~O 

# lor 102 

# 10{ /02 

# /02- 102- 

# toz: /02

(02. 

# 102 (02- Time Port Point**~p** 

### ("H2O) 

### Ts 

### (OF) 

## B 

# 1 

# .ss /02 B 2 

# , o ] IOZ B 

# 3 I 

# q"3 (0'2- B 

# 4 /**~O** 

# 102- B 

# 5 

# ,CJb /03 B 

# 6 

# I ,,0 

# /05 B 

# 7 

# /10 /03 B 

# 8 Jf 

# Cf8 /03 B 

# 9 

# q)" /02 B 

# 10 

# ,Q3 102- B 

# 11 

# ,R8 /02 

# gs-C B 

# 12**~.8r;** 

# qb**('6~)D)** '-



### Use 

## Bwsand MW data from previous Run? Yes No

Time 

# v: (ft") Meter Meter Imp. Out .b.H In 

### (OF) Out 

### (OF) (OF) ("H2O) 

## OCflq 

# 220

..25i 

# 8J 82 

# 57**'j~** 

# 0'124 HZ 

# 82 S5 OQ2Q 

# 4 83 51;:1 

# 'o- 3L 

# b 

# Bl.-f 

# 55 

# OC'.3c 

# 18 

# 8Lf 

# 56**O~ ~'1L**  

# " / 

# 0 

# Rm 5"7 

# .
I'-' 

# 21f

# +
..7b'3 

# q( 87 60 \JV Bws:



# --- Net

Pre-Test Leak Check: 

# c§'i) Post Test Leak Check: t 

## C> () 

# 2 Fail 

# q
e 

### CFM at 

## IV) , "Hg

Form 1012 GE Energy

## Methods 2, 3 & 

## 4 Field Data Sheet Project #: 

### Company: Plant: Source 

### 10': Load: Stack Dim: Stack Area: PitotlD: 

# DO 

# 8 Pitot Cp: , Meter 

### 10: 

# 88750 Meter Y: 

# '0 If

# crMeter AH@i: 

# 1,7/B Operators: 

# 'LWj g 8- Run Number: Page 

# ---I- of 

## _I Date: Pbar ("Hg): Pstatic ("H20): 

# 3

Pre-Test Pitot Leak Check: Pass Fail

Time Port . Point AP ("H2

### 0 ) Ts 

## (oF) 

# th**"-I~'** A 

# 1 

# ,,7/ 

# IOl-f

.**(~** 

# lf5) A 

# 2 

# ,77 JOYA 

## 3 

# aQO 

# lOS A 4 

# .e: 105 A 

# 5 4'

# qa ior; A 

## 6 

# qS i05 A 

## 7 

# ,,9lf.. iDS A 

# 8 

# 4l'95 j

# 0 '--) A 

## 9 

# b93 10.5 A 

# 10 

# q'l 10'5 A 

# 11 

# 189 lOL.{- A 

# 12**~85** 

# Q7' Time Port 

# B B B B B B B B B B B B 

# 1 

# .83 2 

# ,'05 3 

# ,83

9

...

# qs 10 

# 0,0
12 

# ,85 /OZ 103 /03 

# (03 

# 103 (03 

# (04 

# /03 iD3 104 

# /03

Use 

### Bwsand MW 

### data from previous Run? Yes No

Net

Bws:



# --- 2 3 1



## 4 Total Train 

# 12 111

..



## a2. 

# 55 bO 

# 60 

# 9/



# 110 

# aD Time 

# v: (ft") Meter 

# 245"lb5 In 

## (OF)



# 052 

# c I 0 1-12 

# qO Df../.7 qO


# 1/02 

# 26q.58B 00 '037 

# 8'1

Pre-Test Leak Check:

# Cfas~ Post Test Leak Check: # 

## 00 

## 2. Fail ]., CFM at _ 

# Ii1 "Hg

Form 1012 GE Energy

## -0.75 Run Number: Page _,_ of _1_ Date: Pbar ("Hg): Pstatic ("H2

### 0 ): t. 

### 7/'} 

# 008/1 Pitot ID: Pitot Cp: Meter ID: MeterY: Meter**~H@i:** 

### Operators: 

## /6.7/ ' I 

## Cf

## IJj· 

# 'Sl/rA 

# I Project #: Company: Plant: Source ID: Load: Stack Dim: Stack Area:

Pre-Test Pitot Leak Check: 

### Fail

Time Port Point**~p** 

### ("H2O) 

### Ts (oF) 

# r» ';, A 1 b' 

## (j 

# II

# c< A 2
M 

## I ( fIt) 

# A 3 t>

# 7Lf IIi( A 4**.~** 

# l II

# L( A 5**,~~** 

# 1/t{ A 6 f 

# q \ 

# )/« A 7 p 

# 9& i I 

# A 8

.. 91 

# Jf<, A 9 

# .rsq i/( A 

# 10**4g~** 

# if( A 

# 11 '7

# q 1/( A 

# 12 Ie( 

# itO Time Port Point**~p** 

### ("H2O) 

### Ts (oF) 

## B 

# 1**~7'l,** 

# 1/«' B 2

## ~~) 

# /I') B 

# 3 

# , Cf 0 

# lit{ B 

# 4 

# q, r« B 

# 5 

# 1'& j/( B 

# 6 

# 1tfJ I/r B 

# 7 

# "crt 1;( B 

# 8 

# .1') /1 

# t) B 

# 9**i~<d** 

# !Ie B 

# 10 

# ,70 lit; B 

# 11 

# ,,75**//~** 

# If 

# /3 B 

# 12 r 

# "5 

# /oq

Use Bwsand 

## MWdata 

## from previous Run? Yes No

Time 

## V m 

### (ft;j) Meter Meter Imp. Out t.H In (F) Out (OF) (OF) ("H2O) 

# ne» 2.

## Lfi.3 t-f**7~** 7Y 

# 7'7 /**l<l~** 

### '2 

# n»") 7') 

# 7{ v 

# t7 (tl 

## 71 

# 77 )7(" 

# ,I ""7'0 J?**)~** 

# Ib )1 I 

### 171" 

## 7 7 

# 71 '\ 

### \ ( 7 

## ')0 

# ')07, 

# /'71. 77 

# 71 \ / 

# \V \



# 71 78 

# I Imp# 

# I Initial 

# I Final 

# I Net 

# I 1 1

# e« '1 

# :61'1·r 2 "?

### 6 7, 

## J ") 7

## vft.! 3 7 

### I

### t. " 

## 7(LJ 4 "60), [ 

### -tP 1, ( 

### Total Train
Bws:



# ---

Pre-Test Leak Check: 

# @ Post Test Leak Check: 

## ,08 D 

### Fail CFM at 

# /0 "Hg

Form 1012 GE Energy

## Methods 2, 3 

# &4 Field Data Sheet Project 

## #: Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

## SVOJI : 7( Pitot ID: Pitot Cp: Meter ID: MeterY: Meter i1H@i: Operators: 

## 1. 

# n« riAl //(J) 7 

### Run Number:**_~=--** 

## _ Page f of f Date: - 

# -S",LJ;1D Pbar ("Hg):**="J.~"~'():;'-** 

### __ 

### Pstatic ("H20): _-.......::0:..:.....

### ~=-- 

## __

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point i1P ("H2O) 

### Ts (OF) 

# (j

# 7a; A 

# 1 

# t.n 

# "1... A 

# 2 0,41.) 

# If"- A 

# 3 

# ».a» 1/1 A 

# 4**IJ.~** 

# 7 1/3 A 

# 5 

# ,; { 

# "., A 

# 6 t, (**II~** 

## A 

# 7 

# I. " 

# I('f 

## A 

# 8 

# OJ;

# y (f'l A 9 

# vA/ /Ill A 

# 10 

# P

..r"t If

# 'I A 

# 11 I.)).. 

# I(t.J A 

# 12 0·73**~(**

Use 

### Bwsand MW data from previous Run? Yes No

Time 

# v; (fe) Meter Meter Imp. Out LiH In (oF) Out (oF) (oF) ("H2O) 

## [;IfO 

## 1**~"'1.** 

# 01**/~**

### 7~**.e{~~** 

# '2£1 i"J"J 7/) 

## '7/ \ 

# riCO 7'1 7/



## ',il'" 

# '71 ,1 

# " 7/0 

# ?J n 

# \ \ / 'J

# It, )) 71- 

# \ 

# I / 

# 1 J..()

## 2~/. 

# '1Qt 

# '7J ,) \ I

IL Time Port Point i1P ("H2O) 

### Ts (oF) 

## B 

# 1 

# V. (I 

# III B 2 

# d.7t " "J B 

# 3 

# 0. }f 

## II.) 

## B 

# 4 P.fl[ 

# ({'I B 

# 5 

# o. CJS"" IfC( 

## B 

# 6 

# tJJif /It! B 

# 7 

# I,() It 

# If B 8 

# I. C> 

# 1/'1 B 9**().~O** 

# / / 'I B 

# 10 P. Ii1. 

# /1'/ B 

# 11 

# e.**~S-** 

# Ill). 

# 11711 B 

# 12 • ., 7 

# 7'd



# I Imp# 

# I Initial 

# I Final 

# I Net 

# I 1 

## 7q,-/,

# J 7 )../" 

## 2 

# 73b.:2 7:3 

# "6,q 3 

## 74L1- 

# 7 '1').,0 4**'l)~.J,** 

## J**O~I** 

# { Total Train
Bws:



# --- : r



### Pre-Test Leak Check:

# ~ss") Fail Post Test Leak Check: { CFM at ( 

## I

Form 1012 

### "Hg 

# 175

GE Energy

## Methods 2, 3 

# &4 Field Data Sheet Project #: 

### Company: Plant: Source 10: Load: Stack Dim: Stack Area: 

# 1J. 71 Pitot 10: Pitot Cp: Meter 10: MeterY: Meter ilH@i: Operators: 

## I. 7/'6 Run Number:

# --=3~ 

# _ Page 

# -L of 

# .L Date: ("

- 

## f...-o7 Pbar ("Hg): _'14---:..;....!""-(

_ 

### Pstatic ("H2

### 0 ): 

## _-_0._,'O-<.L--

__

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point ilP ("H2O) 

### Ts (oF) 

# IJ} ;')'1 A 

# 1 

# d, 7'1 (fj A 

# 2 ,**l6~** 

# ,,'> A 3 

# , f ( ff{' 

# A 4**,~...,** 

# 115 A 5 .Cj 

## 7 (15 

# A 6**,.~i** 

# u« A 7 

# ·110 (11 

# A 8

## ~~ 

# '4!' A 9 

# .**~,')** 

# tl'f A 

# 10 

# .77 (/1, 

# A 

# 11 

# ,7':>**f~** 

# A 

# 12 

# b(**1~'tJ** 

# I Time 

# I Port 

# I Point 

# I ilP ("H2O) 

# I Ts (oF) 

# I B 

# 1 

# .c« t 

# fl.

... B 2 

# ,7.1.. {('- 

# B 3 t 

# 7

# Y ((2- 

# B 4 .CfJ/; 

# ,(z, B 5 

# l1t't 1(2. 

# B 6**,,~6** ({').. 

# B 7 

# ,**q~**

# 11~ 

# B 8 JtLf 

# 1'11- B 9**,~I** 

## IU

# B 

# 10



# . "51 fld-. 

# B 

# 11 . 1'0 

# r(l

# O?

# JO 

# B 

# 12 

# .77 

# Ill.

Use 

### Bwsand MW data from previous Run? Yes No

Time 

# v;**(ft~)** 

### Meter Meter Imp. Out LlH In 

## (OF) Out (oF) (oF) ("H2O) 

# 1/17 1# 

## {tis. 

# 7('1 

# 74 7 

# s**/(~o-** 

## 2.

'7 )0 

# 715 71
-"7

## t:.-t/I 

## r?-? f:,P 

# , 7 

# «< e;t/**~v** 

# /**7~** Cf,# 

# -&1 I 1/ 

# 17<t7 '6( 

## -6( 

# I l/'6tt(J 

## 1/Qji'lQ 

# CiL..**~.L** 

# 1// IV 

# I Imp# 

# I Initial 

# I Final 

# I Net 

# I 1 /1Lti 

## "/7/JJ 2 

# a« J 7N.'1 3 (p1"- 

## C( 

# b 2/. i; 

## 4 

## (.1 7..

## 6 C'fl. ,- Total Train
Bws:



# ---



# 176 Pass Pre-Test Leak Check: Fail Post Test Leak Check: CFM at "Hg



# ----- ----
Form 1012 GE Energy

## Methods 2, 3 

# &4 Field Data Sheet Project

## #: Company: Plant: Source ID: Load: Stack Dim: Stack Area: 

# 11)..J.A())Y

# 6 Pitot ID:

# H{io~''-7**~':k** PitotCp: 

# l..J,"bbtj**5~)t** Meter ID: 

## £t.,

# rt Sic-d. 

# F

..,.-.,.**:3~** MeterY: 

# ).qd /: Meter**~H@i:** 

## '5' '7 I 

### r 

### Operators: 

## I.oa£, Run Number:

__ 

# 1 _ Page 

# L of 

# I Date: -

## ~/2/o7 Pbar ("Hg): '2.

# IUO Pstatic ("H20): 

### _-_..**e.....s...!a~**

# __

Pre-Test Pitot Leak Check: 

### Fail

Time Port Point**~p** 

### ("H2O) 

### Ts tF) 

## i)l{1 

# A 

# 1 

# i-> /)-.<{ ('11111 

# A 

# 2 07r; IJ---L(

'-- '/ 

# A 3 

# Jt7 JrY A 4**~9g** 

# /)--,-/ A 

# 5 J '" I 

# /J--1 A 

# 6 

# I " I 

# JJ-L, A 

# 7 

# I " 

# I 

# Ire., A 

# 8**,,~** 

# <i J)-l-f A 

# 9 

# I 0 

# J?-<..( A 

# 10 10

# q \ 

# f}-'-f A 

# 11

M

# 7 c:r 

# D-4 A 

# 12 "ft;

# r; /17

Use 

### Bwsand MW data from previous Run? Yes No

Time 

# v; (fe) Meter Meter Imp. Out**~H** 

### In (oF) Out (oF) tF) ("H2O) 

## J(

# "Sl1 

# o·Wf,.**11,.~** 

# 7C 

# flo 

# s> )..'1.

## J~~

## 7~ 

# 7q**4~** 

## ''<'4 

# - '1-1 

# '/9b Lff,.. /1("k"L 

# ,-ItLJ 

# 77 l/f(' 

# Ie.. c;-e11 .;. 

# "7 7(P tfl/ 

# 1v@C{ ";j 

# - " 

# 7cP i/C[ I/(,oq 

# lOflbo).-\ Yf.(



# r I Time 

# I Port 

# I Point 

# I**~p** 

### ("H2O) 

# I Ts (oF) 

# I 8 

# 1 

# &'1 j;)...<{ 8 2

# ~I 

# I?-V 8 3 ct(' 

# I?--'-( 8 4 

# "qtA 

# tJrL( 8 

# 5 / I) 

# I 

# IJrLf 8 6 

# / " )-- 

# 1).--'-1 

# 8 

# 7 

# P(j I'YL{ () 

# 8 

# 8 '" c**~0** 

# I"J-lf 8 9

# ~t**~t&** !')-L( 

# 8 

# 10 

# .1,'1 1

# ?--c.( 8 

# 11 

# ;1C b->

I

# J)'L(Cf 8 

# 12 "f.zo 

# jlr;, 1IL-t0tj;**'~** 

## /

Imp# Initial Final Net 

## 1 

# 7 71 , (. 

## 7Cil.1·Q 2 ',)2Q.1... 

## 70/.0 3 

## 'J,J..II. 0

### ~(~. 

# ? 4**~(l1.J ~/)..,1j**  

### Total Train
Bws:

# .~**()(;~**

Form 1012 

# 7 "Hg 

# :177

GE Energy

## Methods 2, 3 & 4 Field Data Sheet Project

## #: Company: Plant: Source 

## ID: Load: Stack Dim: Stack Area: 

## $·7I ( Pitot ID: Pitot Cp: Meter ID: MeterY: Meter**~H@i:** 

### Operators: Run Number: Page 

## _1_ of _' Date: Pbar ("Hg): Pstatic ("H20):



### Pre-Test Pitot Leak Check: 

### Fail

Time Port Point**~p** 

### ("H2O) 

### Ts (OF)

# /~)~ 

# A 

# 1**~~q** 

# i»

# .> ( is si ) A 

# 2 0/-

## ~Y' 

# /J--')-- A 3 

# Jr**~9** 

# Jr'!? A 4 

# .Gi') 

# n---; A 

# 5 

# /,0 Ir> A 

# 6 

# J

# .:»-: Ir'> A 7**~qq** 

# 1;--> A 

# 8 J

# 6/**)~'-;** 

# A 9 

# .cr7 Iy--'; A 

# 10 

# .9G**Iy~** 

# A 

# 11 

# .e. Ir> A 

# 12 

# .c y 

# /17

Use B 

### wsand MW data from previous Run? Yes No Time Port Point**~p** 

### ("H2O) 

### Ts (OF) 

## B 

# 1 

# 6"7 /'J--

# -S B 2



# ..7Q j')-?:, 

## B 3



# ..B1 /»

# 3 B 

# 4 

# .Cf7 1')--'7, 

## B 

# 5 

# r41**/~3** 

## B 

# 6 

# I I 

## jty3 

## B 

# 7 ,Ie

# '7 / )--';> 

## B 

# 8 Jle

# p7**/r~** 

## B ·9

.. 

# F'; n-'? B 

# 10 

# 11**~7** 

# I?--'!:J 

## B 

# 11 f#

## 7~

# I~ 

# /701 B 

# 12 

# "C;-Cf 

# u«:**v'(~()I)**

. Time 

## V m 

### (ff)



## 17l)..O 170t) 

# 1/'7{0 

# II,')--£) 'I r.y..)O 

# I 

# IY 

# 74 ( I**~H** 

### ("H20) 

### Imp# 

### Initial Final Net 

### 1



## - 7'67.::; 

## 1JPl1 2 

## £ 

# 'iIf. .L

### 7/'J~ 

### ) 

## 3 

## ""1'37.7 

## 7)7.1 4 

## 'jJ'1.( ).p, 

## '3 Total Train


## Bws:



# ---

% CO2:

# I ij. 'j

% O2: 

### f'l

Form 1012 

# :178

GE Energy

## Methods 2, 3 & 

## 4 Field Data Sheet Project#: Company: Plant: . Source ID: Load: Stack Dim: Stack Area: 

# s 71' Pitot ID: Pitot Cp: Meter ID: MeterY: Meter dH@i: Operators: Run Number:

# ~-:r-.J Page ( of 

# If Date: - - 

# 0B/07 Pbar ("Hg): 241. C**----""'-~---** 

### Pstatic ("H2

### 0 ): _---"--'(;

..**'-"~'__** 

### __

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point dP ("H2O) 

### Ts t r-) 

# 7;lt, A 

# 1 

# ,"2 

# 12/**I~** i 

# c) A 

# 2 

# ,'77 / Z I A 

# 3

# J~O 

# IZ ( A 4 

# /,; j

# 2/ A 

# 5 

# 1,2- (2 ) 

# A 6 

# I

.. 

# I / Z

# J A 

# 7 

# I4' 

### J 

# /20 A 8 

# [..0 {20 A 

## 9



# ..9b /20 

# A 

# 10**~q/** 

# [20 A 

# 11 

# 95& f20 A 

# 12



# . ,,72 

# 1// Time Port Point dP ("H2O) 

### Ts (OF) 

# B 

# 1 

# .,.80 12/ B 2 

# ,89 /2 

# J B 3 

# J J1 / 

# /2 ) B 4 

# / "I I 

# Z / B 

# 5 ..:J.

## ~iA3 

# '2/ B 6 J 

# i 2 

# I B 

# 7**~J** 

# i2/ B 

# 8**~qq** 

# (2 

# I B 9


# .. qS- 120 B 

# 10 

# .,83 /20 B 

# 11**~77** 

# /20 

# 7:**~.-')** 

# - B 

# 12 

# .; bJ /oq ( 1_ • 't 7



### Use 

### B

## wsand 

### MW data from previous Run? Yes No

Imp#

Total Train Net Initial Final 

# 8/5

.. 3 

# IEq.o 5/7.. 0**1t:;17..~**



### Bws:



# --- 1 2 3 

## 4 Time 

# v; (W) Meter Meter Imp. Out AH In (OF) Out (OF) (OF) ("H2O) 

## '0720 

# 17

.."3,)2 91**q~** 

# 57 2 

# t« 0725' I 

# 8 

# '-I 

# q/ 5:$ 

# oTJo**R~** 

# 3q S-fo 

# 07JS' 82.. f"'1'"7 

# 57 

# otno , , 

## f1} 

# >-IS 

# 58 

# b745 '\I 

# 18 I 

# 83 5Cf 

# o

# tso /CfS,,'!b2 

# Bi 

# 83 

# bO \V

Pre-Test Leak Check: Fail 

# r " Post Test Leak Check: -I<1J_oDLr"=---:...

__ 

### CFM at 

# o [h.. "Hg 

# :179

Form 1012 GE EnergyControl Module No. Standard MeterNo. Standard Meter (Yr) 38758 13124821

0.994 

## Pre TestDGM Calibration

Date: Calibrated By: Barometric Pressure: March 1, 2007 VT 28.63

Run Number Orifice Setting in. H20

(set value) Orifice Setting in. H20

(read value) Standard Meter Volume

Vr Control Module DGMVolume Vd Standard Meter Temp. F
tr Dry Gas Meter Inlet Temp. 

### F tdi Dry Gas Meter OutletTemp. F tdo Dry Gas Meter Avg. Temp. F td Time Min. Time Sec. Y**~H@**

Initial 718.324 434.409 66 71 70 Final 723.409 439.500 66 71 70 Difference 1 1 0.81 0.80 5.085 5.091 66 71 70 70.51 91 43 1 1.005 

# I 1.686 Initial 713.323 429.405 66 71 70 Final 718.324 434.409 66 71 70 Difference 2 1 1.61 1.60 5.001 5.004 66 71 70 70.5 

# I 61 561 1.004 

# I 1.775 Initial 708.000 424.102 66 71 69 Final 713.323 429.405 66 70 70 Difference 3 \ 2.41 2.40 5.323 5.303 66 70.5 69.5 70 

# I 5\ 53 

# I 1.005 \ 1.694
Specifications: CFR 40, Part 60, Appendix A, Method 5, section 10.3.1. CalibrationBefore Use. 

### Pre TestCalibration Factor (Y) 1.005 1.718

### ~b 

# C«J 

# o

GE Energy 38758 03-01-07.xls

## PITOT TUBE CALIBRATION
UNIT: 008 CALIBRATED BY: IS DATE: 12/12/06
A SIDE CALIBRATION dPstd dP(s) DEVIATION RUN No. "H2O "H2O CP(s) Cp(s)-Cp(A) 1 0.58 0.80 0.843 0.003 2 0.58 .•.. 0,81 0.838 0.002 3 0.58 0.81·· 0.838 0.002 Cp(A) 0.840

B SIDE CALIBRATION dPstd dP(s) DEVIATION RUN No. "H2O "H2O CP(s) Cp(s)-Cp(B) 1 > 

## 0.58 0.81 0.838 0.000 2 ..; 

# . 0.58

........ p.a1 0.838 0.000 3 ., 

## 0.58 0.a1 0.838 0.000 Cp(B) 0.838 Avg Deviation A must be less than or equal to 0.01 Avg Deviation B must be less than or equal to 0.01 ICp(A)-Cp(B)1 must be less than or equal to 0.01

Avg Deviation (A): Avg Deviation (B): 0.00 0.00 

# ICp(A)-Cp(B) 

## Cp 0.00 

## 0.839



# :181.

### Project: FSR: Model: 

### SIN: Date: Run#

Time


## 11:10 11:11 11:12 11:13 11:14 11:15 11:16 11:17 11:18 11:19 11:20 11:21 11:22 11:23 11:24 11:25 11:26 11:27 11:28 11:29 11:30 11:31 11:32 11:33 11:34 11:35 11:36 11:37 11:38 11:39 NOx Peak: NOx Final: Allowable Minimum: Pass/Fail: Number of Scans: Hibbing Taconite M22A0346 TECO 42C 42CHL·75089·378 

### 4/11/2007 NOx Converter Check
NOx 

### (ppm)


## 41.76 41.76 41.76 41.77 41.78 41.79 41.78 41.78 41.78 41.77 41.77 41.77 41.77 41.77 41.79 41.79 41.78 41.78 41.78 41.79 41.79 41.79 41.78 41.79 41.78 41.78 41.78 41.79 41.80 41.78 41.80 41.76 40.97 PASS



## 30



# :182

### +248-589-2134 SCOTT SPECIALTY GAS 

### 484 P01 MAR 12 

### '0'7 10:29**K~.""** 

# •.•. A

...... 

# -.. 

# IIScottSpeclalty Gases**Dual-Analy~ed** 

# CalibtadtJ# $t(llldard

I .29,0 COMBERMERE 

### STREEUROY.MJ 48083 

### PhOfl6: 249-68Q·2960 ·fBX: i4i3·589·2131l

.' '. 

# C.ERTIFICATE OFACCURACY: EPA Protocol Gas



# - -

.

.. 

## !'Nay LaboratorY 

### CwrtomsJ P.O. No.; MPEAGAN010207JJT02 

### GE ENERGVIELMURST SCOTT SPECIALTV GASES 

### Project No.: 

### 05-61095-001 1290 COMBERMERE STREET 888 INDUSTRIAL DRIVE TROYIMI 

### 480S3 eLMHURST 

### JL. 60126·1012 

### ANALmeAl.. INfORMATION 

# . Thill 

### esrtlflclltlon W81J perforMed according 

### to EPA Traceilllliity 

### ProtwoJ for 

### AUDy & 

### Cartifloation of Ga$OOUll 

### Calibration Standat'd8; Procedure 

### G-,; 

### september, 1"9"97. 

### CyUnder Number: ALM020950 

## CerttrlCBtIon Date: 

### 24Jan2007 

### Exp. Date: 

## 23Jan20l0 Cvlinder Pre$lIureH iI : 

### '900 PSIG 

### ANAl.YTICAL CQMPONeN.J PERTIFIED 

### CONCENTRATION (MoJss) 

# ACCURACY" TRACEA81LiTV CARBON OIOXIDE 

# '.858 % 

### +1· 1% Direct NIST Md 

### NMI OXYGEN 

# una % +/- 

### 1% 

### Direct NIST and NMi**NIT~OGEN** 

### BALANC£

... Del nQl UBI! when Il)'Undef pre5$\Ire .15 bBlow 160 I)lllg,

•• Analrtic;tl IQIlUlllCY is 1I11asd on the r.9ulrlltnllntli of EPA Prot6CoI P10cedure 61.**8epteml)~r** 19$7. 

### AeFEReNCE SfANOARD TYntSRM

## .W!. "EXPiRATlgN OM!

.

### CYL~ 

## NUMBER CONCF14Tf!AliON 

### COMPONINT**23~ CO~1N2**  01NClY2010 10002807 23.04 96 CAAaDN OIOXlOe**~TRM** 2350 01Mav2000 IC028!i42 23•.48 '110 

### OXYGeN


### INSTRUMENTATION**~TRUMEN1IMODE1JSERtAI,,!,** 

### Q!TE lAS! CA1.J8fIA:n:D Arw.rrICAL PRINClPLl VAAIANI3400110893**Q3J~2007** THEIWAl CONDUCTIVITY**CALiFOANIA/ll0P/SO~41** 11Jan2007 PARAtMGNiTfC



## ANALYZER READINGS


# . tZ =0

### Zero Gas R

# =RefelllrtceGas 

## T:Test·Gas r'"Correlation Coefficient) FirstTnad Analysb 

## s.eond Triad Analvsls Callhratlon CUrvll

CARBON D10XfDE . lIlID; Z2.ton2llD-7 ··IloIIlaow.· Unlr:WA. 

# I" 

# ] Co_1OIl-A+8N"Ca2+tls3 +&4 Zl·0.000OO 1'11

..."84106. T1,,$03966.0 r.z'O;ll$VH1 RlZ-111181OO. Z2.0.llOOOD U"S02A2S.cJ e-tInlIl A-·0.036$04

.**~3-0.QOOOO** 

### :u -1111:147.0 IU.. ".,1100. I-O.OOOO2ll 

## e-o

Avu. C_lauOll' 11.11118 .". 'IhO J!'!O
_u........., II.,**2I~** ...:Z0ll7 "-'110- llIIlt!'lIo 

# [ I ...**aOll~-A+Ix+C>l2+Dd+&4** ·Z1wO.DOOOO 111 -"2I.4lIQOa 11"'·&.&2OOtl· r-0.818"8 lit

...13••1011O**~2.=O.olllOll** TZ-,JlllOOO QIRdIIIb: 

## "-o.lIom,,, Z3-0.Dl000 n-9.BZIlOO M=2S ...7OOD ,,.O.lIllS$70 

## C-o
AWl. e-lu.tl"", '11.11' 'I/o 0-0 /1=0



### APPROV£O BY:

# JIJ:~ 

# -

-

# .. :183AftJ.ft • .• ,..... "., 

## Dual-Analyzed Calibration Standard 

# I. Scott Specialty Gases

••' 290 COMBERMERE STREET,TROY,MI 48083 Phone: 248-589-2950 Fax: 248-589-2134

TM 

# CERTIFICATE OF ACCURACY: Interference Free Multi-Component EPA Protocol Gas
Assay Laboratory SCOTT SPECIALTY GASES 1290 COMBERMERE STREET TROY,MI 48083



### ANALYTICAL INFORMATION P.O. No.: MP-EAGAN-060206JJT02 Project No.: 05-44270-001 Customer GE ENERGY/EAGAN CAMPUS PHASE 1 1301 CORPORATE CENTER DR SUITE 177 EAGAN MN 55121-0887

This certification was performed according to EPA Traceability Protocol For Assay & Certification of Gaseous Calibration Standards; Procedure G-1; September, 1997. 

### Cylinder Number: ALM025173 Certification Date: 19Jun2006 Exp. Date: 18Jun2008 Cylinder Pressure***: 1835 PSIG CERTIFIED CONCENTRATION (Moles) 

### 10.99 

## % 226.7 PPM 21B.l 

### PPM 226.2 PPM BALANCE COMPONENT CARBON DIOXIDE CARBON MONOXIDE NITRIC OXIDE SULFUR DIOXIDE 

### * NITROGEN - OXYGEN FREE TOTAL OXIDES OF NITROGEN 

### 218.4 PPM ACCURACY** 

### +/- 

## 1% +/- 1

### % +/- 1

### % s.]: 

### 1% TRACEABILITY Direct NIST and NMi Direct NIST and NMi Direct NIST and NMi Direct NIST and NMi
Reference Value Only

••• Do not use when cylinder pressure is below 150 psig.

•• Analvtlcal accuracy is based on the requirements of EPA Protocol Procedure G1, September 1997. • This Protocol has been certified using corrected NIST S02 standard values, per EPA guidance dated 7/24/96 and will not correlate with uncorrected P t 

### REFERENCE STANDARD TYPE/SRM NO. EXPIRATION DATE NTRM 2000 01Jul2009 NTRM 1680 01Nov2008 NTRM 1685 01Jan2010 NTRM 0260 01 May2008 

### INSTRUMENTATION INSTRUMENT/MODELISERIAL# FTIRII0928621 HORIBA/A1A-220/57297601 FTIRII0928621 FTIRII0928621 CYLINDER NUMBER K025974 AAL 18386 AAL071058 ALM019186 CONCENTRATION 5.006 % 498.0 PPM 246.1 PPM 254.4 PPM

DATE LAST CALIBRATED 25May2006 07Jun2006 08Jun2006 05Jun2006 COMPONENT CARBON DIOXIDE CARBON MONOXIDE NITRIC OXIDE SULFUR DIOXIDE

ANALYTICAL PRINCIPLE FTIR NDIR FTIR FTIR 

### ANALYZER READINGS

First Triad Analysis 

### IZ-Zero Gas R-Reference Gas T -lest Gas Second Triad Analysis 

### r - Correlation Coefficient) Calibration Curve

A =O.OOOOOE+ 0 C

## =8.26800E-3 E=O.OOOOOE +0

A=-0.303658 C=0.000938 E=O

A=O.OOOOOE +0 C=4.40000E-5 E-O.OOOOOE +0 CARBON DIOXIDE Date: 12Jun2006 Response Unit: % Zl =-0.00065 Rl = 17.87561 T1 = 10.98771 R2 = 17.88010 Z2 =-0.00008 T2 = 10.99628 Z3 =0.00202 T3 = 10.99786 R3 = 17.88754 Avg. Concentration: 10.99 % CARBON MONOXIDE Date: 13Jun2006 Response Unlt:MV Z1 =0.00000 R1 =150.0000 T1 =75.50000 R2= 150. 1000 Z2 =0.00000 T2 = 75.60000 Z3=0.00000 T3=75.60000 R3=150.1000 Avg. Concentration: 226.6 PPM NITRIC OXIDE Date: 12Jun2006 Response Unit:PPM Z1 =-0.19566 R1 =502.2254 T1 =219.1753 R2=502.3991 l2=-0.09408 T2=220.4931 Z3 = 0.01 846 T3 = 220. 7702 R3= 503.8373 Avg. Concentration: 217.9 PPM Date: 19Jun2006 Response Unit: % Zl**~-0.00056** R1 =5.03714 T1 =10.97136 R2=5.03758 Z2=0.00072 T2=10.98139 Z3=0.00139 T3 = 10.99067 R3 - 5.04347 Avg. Concentration: 10.91 %

Date: 21Jun2006 Response Unit: MV Z1 =0.00000 Rl =150.1000 T1 =75.70000 R2= 160.2000 Z2 = 0.00000 T2 = 75.70000 Z3=0.00000 T3=75.60000 R3=150.0000 Avg. Concentration: 226.8 PPM

Date: 19Jun2006 Response Unit: PPM Z1 =-0.11745 Rl =248.2863 T1 =220.2458 R2=248.6055 Z2=-0.07368 T2=220.4113 l3=-0.04273 T3=220.4663 R3=248.7018 Avg. Concentration: 218.2 PPM

n. 1**.~.,** Concentration =A+ Bx+Cx2+ Dx3+Ex4 r-9.99982E-1 Constants: B= 7.93236E-1 D = 4.00000E-6

Concentration = A + Bx+ Cx2 + Dx3 + Ex4 r=0.999989 Constants: B=2.848888 D=0.000015

Concentration = A + Bx+ Cx2 + Dx3 + Ex4 r=9.99993E-1 Constants: B = 9.90736E-l D=O.OOOOOE+O

## Dual-Analyzed Calibration Standard 

# Scott Specialty Gases

1290 COMBERMERE STREET,TROY,MI 48083 Phone: 248-589-2950 Fax: 248-589-2134


## CERTIFICATE OF ACCURACY: Interference FreE!"M Multi-Component EPA Protocol Gas
Assay Laboratory SCOTT SPECIALTY GASES 1290 COMBERMERE STREET TROY,MI 48083



### ANALYTICAL INFORMATION Customer P.O. No.: MP-EAGAN-060206JJT02 GE ENERGY/EAGAN Project No.: 05-44270-001 CAMPUS PHASE 1 1301 CORPORATE CENTER DR SUITE 177 EAGAN MN 55121-0887

This certification was performed according to EPA Traceability Protocol For Assay 

### & Certification of Gaseous Calibration Standards; Procedure G-1; September, 1997. 

### Cylinder Number: ALM025173 Certification Date: 19Jun2006 Exp. Date: 18Jun2008 Cylinder Pressure***: 1835 PSIG 

### ANALYZER READINGS lZ-Zero Gas R-Reference Gas T - Test Gas r - Correlation Coefficientl

A = O.OOOOOE+ 0 C=O.OOOOOE+O E=O.OOOOOE+O First Triad Analysis SULFUR DIOXIDE 

## * Date: 12Jun2006 Response Unit:PPM Z1 =0.01016 R1 =509.9225 T1 =228.9517 R2=510.5063 Z2=0.02078 T2=229.2624 Z3=0.02743 T3=229.6671 R3=510.7232 Avg. Concentration: 227.2 PPM Second Triad Analysis

Date: 19Jun2006 Response Unit: PPM Zl =-0.05771 R1 =258.0635 T1 =228.2379 R2=258.1209 Z2=-0.00986 T2=228.3504 Z3 =-0.00153 T3 = 228.6706 R3= 258.1500 Avg. Concentration: 225.1 PPM Calibration Curve

Concentration = A + Bx+ Cx2 + Dx3 + Ex4 r=9.99973E-1 Constants: B= 1.00090E+0 D=O.OOOOOE+O



### APPROVED BY:**_------,=~=.....,....,;-------** 

# 185

# Scott Specialty Gases Dual-Analyzed Calibration Standard

1290 COMBERMERE STREET,TROY,MI 48083


## CERTIFICATE OF ACCURACY: EPA Protocol Gas Phone: 248-589-2950 Fax: 248-589-2134



### Assay Laboratory SCOTT SPECIALTY GASES 1290 COMBERMERE STREET TROY,MI 48083



### ANALYTICAL INFORMATION Customer P.O. No.: MPEAGAN-060305JJT01GE ENERGY/EAGAN Project No.: 05-32127-002 CAMPUS PHASE 1 1301 CORPORATE CENTER DR SUITE 177 EAGAN MN 55121-0887

This certification was performed according to EPA Traceability Protocol For Assay & Certification of Gaseous Calibration Standards; Procedure G-1; September, 1997. 

### Cylinder Number: ALM016371 Certification Date: 23Jun2005 Exp. Date: 23Jun2007 Cylinder Pressure* * *: 1900 PSIG CERTIFIED CONCENTRATION (Moles) 

### 17.41 

## % 428.3 

### PPM 

### 413.0 PPM 

### 419.3 PPM BALANCE COMPONENT CARBON DIoXIDE CARBON MONOXIDE NITRIC OXIDE SULFUR DIOXIDE 

### * NITROGEN - OXYGEN FREE TOTAL OXIDES OF NITROGEN 

### 413.0 PPM ACCURACY** 

### +/- 1

## % +/- 1 

### % 

## «t- 1% 

### +/- 1 

### % TRACEABILITY Direct NIST and NMi Direct NIST and NMi Direct NIST and NMi Direct NIST and NMi Reference Value Only

••• Do not use when cylinder pressure is below 150 psig.

•• Analvtlcal accuracy is based on the requirements of EPA Protocol Procedure G1, September 1997 . • This Protocol has been cenified using corrected NIST S02 standard values, per EPA guidance dated 7/24/96 and will not correlate with uncorrected Protocols. 

### REFERENCE STANDARD TYPE/SRM NO. EXPIRAnON DATE NTRM 1675 04Ju/2008 NTRM 1680 01Mar2007 NTRM 1687 01Feb2007 NTRM 1661 01Aug2007 

### INSTRUMENTATION INSTRUMENTIMODEL/SERIAL# MKS FTIR/2030/0928621 HORIBAIA1A-220/57297601 MKS FTIR/2030/0928621 MKS FTIR/2030/0928621 CYLINDER NUMBER K003719 ALM065546 AAL0678561 ALM022576 CONCENTRATION 13.93 % 486.3 PPM 976.5 PPM 493.8 PPM

DATE LAST CALIBRATED 18Jun2005 08Jun2005 18Jun2005 18Jun2005 COMPONENT CARBON DIOXIDE CARBON MONOXIDE NITRIC OXIDE SULFURDIOXIDE

ANALYTICAL PRINCIPLE FTIR NDIR FTIR FTiR 

### ANALYZER READINGS

First Triad Analysis 

### (Z - Zero Gas R- Reference Gas T - Test Gas
Second Triad Analysis 

### r - Correlation Coefficient)
Calibration Curve

A=O.OO C=3.86000E-3 E=O.OO

A =0.457277 C=0.003395 E=O.OO

A=O.OO C=4.50000E·5 E=O.OO CARBON DIOXIDE Date: 14Jun2005 Response Unit:% Zl ;0.00120 Rl = 13.88187 

### r t = 17.34561 R2=13.88424 Z2=0.00489 T2=17.35018 Z3 =0.00722 T3 = 17.35956 R3= 13.89780 Avg. Concentration: 17.41 % CARBON MONOXIDE Date: 16Jun2005 Response Unit:MV**Zl~O.OooOO** Rl=149.8000 n=134.1000 R2 = 149.8000 Z2=0.00000 T2 = 134.2000 Z3=0.00000 T3=134.2000 R3=149.7000 Avg. Concentration: 428.3 PPM NITRIC OXIDE Date: 14Jun2005 Response Unit:PPM Zl =0.14225 Rl =477.7355 

### r t =409.1452 R2=477.7454 Z2=0.25034 T2=413.0579 Z3 =0.26757 T3=414.5773 R3=477.9985 Avg. Concentration: 413.0 PPM Date: 23Jun2005 Response Unit: PPM Zl =0.00000 Rl =149.9000 

### r t =134,2000 R2= 150.0000 Z2 =0.00000 T2 = 134. 1000 Z3=0.00000 T3=134.2000 R3=149.8000 Avg. Concentration: 427.9 PPM

Date: 21Jun2005 Response Unit: PPM Z1 =0.05298 Rl =477.6738 

## rt =415.3056 R2=477.6852 Z2=0.18848 T2=415.4881 Z3=0.22091 T3=415.7667 R3=477.7481 Avg. Concentration: 416.4 PPM Concentration = A + Bx+ Cx2 + Dx3 + Ex4 r=0.999990 Constants: B=1.00862 

## o=2.10000E-5

Concentration = A + Bx+ Cx2 + Dx3 + Ex4 r=0.999990 Constants: B=2.728123 0=0.00

Concentration = A + Bx+ Cx2+ Dx3 + Ex4 r=0.999990 Constants: 8=1.00234E+0 0=0.00

# Dual-Analyzed Calibration Standard 

# Scott Specialty Gases
1290 COMBERMERE STREET,TROY,MI48083


## CERTIFICATE OF ACCURACY: EPA Protocol Gas Phone: 248-589-2950 Fax: 248-589-2134



### Assay Laboratory SCOTT SPECIALTY GASES 1290 COMBERMERE STREET TROY,MI 48083



### ANALYTICAL INFORMATION Customer P.O. No.: MPEAGAN-060305JJT01GE ENERGY/EAGAN Project No.: 05-32127-002 CAMPUS PHASE 1 1301 CORPORATE CENTER DR SUITE 177 EAGAN MN 55121-0887

This certification was performed according to EPATraceability Protocol For Assay & Certification of Gaseous Calibration Standards; Procedure G-1; September, 1997. 

### Cylinder Number: ALM016371 Certification Date: 23Jun2005 Exp. Date: 23Jun2007 Cylinder Pressure***: 1900 PSIG 

### ANALYZER READINGS (Z - 

## Zero Gas R- Reference Gas 

### T

- Test Gas r - Correlation Coefficient)

A=O.OO C= 1.80000E-5 E=O.OO First Triad Analysis SULFUR DIOXIDE 

### * Date: 14Jun2005 . Response Unit:PPM ZI =0.00684 Rl =494.8579 Tl =420.2873 R2=495.3361 Z2=0.19962 T2=420.5162 Z3=0.22404 T3=420.6669 R3=495.3444 Avg. Concentration: 419.3 PPM Second Triad Analysis

Date: 21Jun2005 Response Unit: PPM ZI =0.00337 Rl =981.7187 Tl =418.3318 R2=962.4368 Z2=0.31568 T2=418.7144 Z3=0.31985 T3=418.8622 R3=962.6088 Avg. Concentration: 419.5 PPM Calibration Curve

Concentration = A + Bx + Cx2 + Dx3 + Ex4 r=0.999990 Constants: B= 1.00054E +0 D=O.OO



### APPROVED BY:

## Message Tryba, James J (GE Infra, Energy)
From: Hayden, Andrea J [ajhayden@cleveland-cliffs.com] 

### Sent: Thursday, May 03,200710:43 AM 

## To: Tryba, James J (GE Infra, Energy) 

### Subject: FW: Test Plan Approval
FYI:



### From: Place, Andrew [mailto:Andrew.Place@state.mn.us] 

## Sent: Thursday, May 03, 2007 10:03 AM 

## To: Hayden, Andrea

## J Cc: Randall, Bruce C (GE Infra, Energy); Beresford, Robert 

## Subject: Test Plan Approval 

## Page I ofI

The test plan approval forms associated with the upcoming NOx performance tests on GP003 Furnace Stacks are included with this message. 

### Please use the forms attached as the Operating Data Summary forms have recently been updated.
Use the Performance Test Report Completeness Criteria form to review the test report prior to submitting it to the agency. The form was designed to help assure completeness of test reports and aid in efficient MPCA report review and compliance determination. It may be helpful to review the PTRCC prior to the test date in orderto be prepared for supplying all the needed information to the test company on the day of the test. This will aid the test company in compiling a complete test report. If you have problems with any of the attachments feel free to contact me. Additional forms are provided at www.pca.state.mn.us/air/performancetest.html Sincerely, AndyPlace Performance Test Coordinator Minnesota Pollution Control Agency 520 Lafayette Road St. Paul, MN 55155-4194 (651) 296-7169



## This electronic message and any attachments included with this message are for the exclusiveuse ofthe individual or entity to which it is intended to be addressed. This message may contain informationthat is privileged orconfidential and thereby exempt andprotected from unauthorized disclosure under applicable law. Ifthe reader ofthis message is not the intendedrecipient, or an employee or agent responsible for delivering the messageto the intended recipient, be aware that any disclosure, dissemination, distribution or copying ofthis communication, or the use ofits contents, is not authorized and is strictly prohibited. Ifyou have received this communication and are not the intended recipient, please notify the sender immediately and permanently delete the original message from your e-mail system.



# 1.88

5/29/2007

## ... ...

# --~.' Minnesota Pollution Control Agency

# 'Perforlt1ance.Tesf.·Phl~.Appro-\ral··· MinncsotaPollutionControlAgcncy ....•. '.,:i 

## 520

## Lafayettel~.d.N;SaintiPaul,MN 551?5-4194(651)

## 296~6~OO www.pca.state.mn.us 

## AQ#541 Facility Name: Hibbing Taconite Company 

## Facility Contact: Andrea Hayden, Section Manager-Environmental 

## Address: Highway 5 North, P.O. Box 589, Hibbing, 

## MN 55746 

## Phone: (218) 262-6856 

## Emission Unit(s): PelletIndurating Furnace Stacks (GP003/SV021-SV032) for BART analysis and Line 

## I Furnace Stack (SV021-SV024) for NOx variablity 

## ScheduledFor: April 30, 2007, 

## atyourFacility located in Hibbing, 

## Minnesota.
Yourtestplan submitted on April 30, 2007, and discussed on May 1,2007, has been approved by the MinnesotaPollution ControlAgency (MPCA) as follows: 

# D Shortenedtest notification approved 

# IZI Test plan approved withoutmodification 

# D Test plan approved with the following provisions:
Include greenball feedrate (feedto grate), fired pellet production rate, and time ofoperation duringtest. Rates can be summarized in "per hour" measurements with supporting data included in test report.
Include FacilityName, AQ File No., Source Designatoras listed in permit (EUOOO, SVOOO, GPOOO, etc.), and TestDate on the face ofthe CD copy.
Please complete Performance Test ReportCompleteness Criteria checklistto ensure all required information is included in the report and inproper sections ofthe report. Make certain all applicable limits and citations are part ofthe results summary ofthe report.


## Attached Forms: 

# D Operating Data Summary- Waste Combustors Operating Data Summary- AsphaltPlants Microfiche/CD-ROM Submittal Form 

# IZI OperatingData Summary- Combustion Sources 

# IZI Operating Data Summary- Process Sources 

# D IZI Certifications Form 

# IZI IZI PerformanceTest ReportCompleteness Criteria
Note: Forms are also available at: www.pca.state.mn.us/air/performancetest.html 

## Approved by: Date: May 3, 2007

Andrew Place Performance Test Coordinator Compliance and Enforcement Section Industrial Division


## Please contact me at (651) 296-7169 ifyou have any questions regarding this approval.


# 1.89

### Please be aware that enforcementaction will be taken forperformance test failures indicating emissions above applicable limits (excess actual emissions to the environment). Failures commonly result in assessmentof a monetarypenalty. Upon thefirst test failure, the Company shouldtake immediate measures to minimize emissions. The measures taken shouldbe documented, as they will becomepartof the recordof corrective actions.
HardCopy Performance TestReports andMicrofiche or CD Copy submittals will be addressedto: Compliance Tracking Coordinator, Compliance andEnforcement Unit, IndustrialDivision, Minnesota Pollution Control Agency, 520 Lafayette Road North, St. Paul, Minnesota 55155-4194

cc: 

### Bruce Randall, GE Energy (email) Bob Beresford, MPCA (email) AQ Corrspondence File No. 541



# :190

# Test Plan for Taconite Ore StraightGrate Pelletizing Furnace Test for NOx

Part I: General Information


## 1. Name and address ofemission facility: Hibbing Taconite Company Highway 5 North P.O. Box 589 Hibbing, MN 55746
2. Emissionfacility contact person: Andrea 1.

## Hayden Section Manager - Environmental Phone: (218) 262-6856 Fax: (218) 262-6877
3. PermitNumber / AQD File Number: 13700061-002 4. Purpose forperformancetesting: a. To quantify NOx emissions for use in the 2007-2011 Air EmissionInventories. b. To provide quantitative data for BART Analysis regarding potentialNOx reductions due to three Energy and Emission ReductionProjects (Combustion ChamberUpperAir InletModifications) performed at Hibbing Taconite Company on Furnace Lines 1, 2 and 3 during 2005 and 2006. 5. Schematic drawing ofstack and sampleports: See Appendix A
6. Locationofplant: Hibbing Taconite Company 2 miles West ofHwy 5 N Hibbing, MN 55746
7. Contractedtesting company information: GE Energy Management Services, Inc. 1301 Corporate CenterDrive - Suite 177 Eagan, MN 55121 Contact: Bruce Randall, MN Regional Manager Phone: (651) 686-0700, extension 16 Fax: (651) 686-4434



# 191. Page 1 of4

## Part II. TestingRequirements
1. The following is a description ofeach pollutantto be tested, the applicable emission limits, and the applicable rule orregulationfor each emission limit:
EU#! Process Pollutant EmissionLimit ApplicableRule orRegulation SV# Equipment Description
Pellet EU 020-022 Indurating NOx No limit NA SV 021-032 Furnaces 1,2, or3

2. The following is a detailed description ofthe fuel samplingprocedure for each pelletizing furnace: 

# F" 

# CJ.i N Natural gas will be used during testing. The EPA "Fd" factor used in emission calculations will be that referenced in Code ofFederal Regulation, Title 40 Part 60, Appendix A, Method 19 - Table 19-2.



## Part III. Operating Conditions 1. Processes to be tested and control equipmentmonitored: L L 

## EU#! ProcessEquipment Maximum ..... 

## ControlEquipment 

# Control'EquipmentOperating Parametersduring Fuel

... 

## SV# Description DesignCapacity Description Testing and how Monitored and Recorded Burned 430 dry short Venturi wet Venturi scrubbers - average ofcontinuous pressure Natural EU 020-022 PelletIndurating tons ofpellets scrubber! drop readings across the venturi and demistpanels, Gas SV 021-032 Furnaces 1,2, or 3 per hour Multiclone and water flow rate. Multiclone - average of continuous pressure drop readings.

Page 2 of4

## The following informationwill be recorded during the test and submitted with the test report: A. 

## Processing rate and total amountofproductmade during each run (by weight). B. 

## Amountand type ofraw material used during each run (by weight). C. Amountofnatural gas used during each run (by volume) (indurating furnace only). D. Dust collectoroperatingparameters. E. Descriptionand date oflast maintenance work done before the test. F. Record keeping ofoperational parameters as measured during the test. G. Calculations. H. Certificationofthe data by aresponsible party.

2. Explanation ofwhy the proposed test conditions are consideredto be worst case in accordance with MN Rule 7017.2025, Subp. 2: For all emissions units, testing will beperformed while the units operate atpractical maximum capacity as conditions allow during the test period.
Part IV. TestMethods


## 1. Listed belowin Section2 are the methods to be used for this test. 2. The following is a description ofthe number oftestruns, length oftestruns, and sampling rate for each pollutant.



# C.D W A. 

## EPA Method 1 for locationofsamplingports and locationoftraversepoints. A single run ofthis method will beperformedto determine traversepointlocations and evaluate cyclonic flow conditions at each emissionpointprior to the performance ofthe remaining test methods.
B. 

## EPA Method 2 for duct velocity and volumetric flow rate. Three determinations: one measurementconcurrently with each test run for NOx at each emissionpoint.
C. EPA Method 3 for fixed gas analysis on combustion sources. One test run on an integrated sample collected concurrentlywith each test run for NOx at each emissionpoint.
D. EPA Method 4 for the determination ofmoisture in the flue gas. One test run concurrently with each test run for NOx at each emission point. Approximate sample rate of0.75 CFM, approximate sample time of30 minutes.
E. EPA Method 7E for NOx. Three sample runs will be conductedwith a sample time of60 minutes at each emissionpoint.

Page 3 of4

# v. Other
1. Gaseous pollutants, in this case NOx, will be reported in terms ofconcentrations (PPMdry) 

## and emissionrate (#/MMBtu & 

## #/hr).
2. Test schedule: See Attachment B.



# ... r..D

Page 4 of4

## May 31,2007
Ms. Andrea Hayden Hibbing Taconite Company Highway 5 North Hibbing, MN 55746-0589
Dear Ms. Hayden: Enclosed are five (5) copies of the report for the NOx

## Emission Study performed by GE Energy Management Services, Inc. (GE Energy) on Multiple Emission Sources at the Hibbing Taconite Faciity in Hibbing, Minnesota on May 1-8,2007. As you are aware, it is your responsibility to submit one copy of this report to the MPCA. Before doing so, please arrange for the authorized person at your facility to sign Item 4 on the "Certifications Required for Performance Test Reports" page located inside the front cover. If we are responsible for generating the MPCA-required electronic copy of this report, please return a signed copy of said page to us at your earliest convenience. If you have any questions regarding this report, please let us know. We appreciate the opportunity to provide you with our services. Sincerely, GE ENERGY MANAGEMENT SERVICES, INC.

James Tryba Senior Project Manager
Enclosure: Five (5) copies, GE Energy Project M22A0346B