NOx EMISSIONS STUDY

Performed At

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

ReportSubmittal Date

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

Performed At

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

Report No.

GE Energy Management Services, Inc. Report M22A03468

Revision 1 - November 1, 2007

Report Submittal Date

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 of the 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 laboratory analysis of field

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 VQVJWlc:'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 SUMMARY AND 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 QUALITY ASSURANCE 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:

Stack Vent 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. Stack Vent 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

Stack Vent 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 Specific

Methods, 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 EnergyProjectM22A0346B 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 recorded

via 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 NOx 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

NOx Concentration 100.9

NOx 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) I Average 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

Minnesota Pollution Control Agency

520 Lafayette Rd. N. Saint Paul, MN 55155-4194(651)-296-6300

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

Company Name: Hibbing Taconite 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, if applicable. 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. Operating Data for Furnace and Air Pollution Control Equipment:

1. Were the furnace(s) and control equipment operated consistent with normal procedures? YES

2, Date(s) and procedure(s) of last maintenance/cleaning within 6 months: January 25, 2007-February 11,2007

3. Include a copy of chart/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 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 of APe 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: Numberand identity of orcrating field(s)

APCequipment and 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-air pollution control Btu-british thermal units gpm.-gallons per minute in. w.c.-inches of watercolumn

lbs.-pounds MW-megawatts psig-pressure persquareinchgauge dP- pressuredrop

23

Page 2 of3
Examples ofAPe 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 identityof operating field(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 Water Flow Rate Minimum (gpm) 649 661 658 656

SV024 Water Flow Rate Average (gpm) 655 667 662 661

Abbreviations: APe-air pollutioncontrol Btu.-british thermalunits gpm.-gallons per minute in. w.c.-inches of watercolumn

Ibs.-pounds MW-megawatts psig-pressure per 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: Thisform provides only a summary ofthe operating conditions during the performance test. Additional and more detailed

records are required to meet the requirements ofMinn. R. 7017.2035. Thisform is to be submitted as part ofthe 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' Saiht Paul, MN 5515?~4194(65n:.29~-~300

'~." ': -: !·Q~~~@!i~·~ •.•••.I>~!a.·.Su~~~ry ••.~~r ••.·coni.·~lis·ti~.~.·.···.S~lI.~.~.e~ •••:::: . Mlnnesot~:· '::

~olilJtlor1.

Control .••

Agenc:}1

Test Date(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 combustion process during the test period.

Attach ultimate/proximate analysis ofthe fuel, if applicable. LIST APPROPRIATE UNITS.

~~ni#& ··:····:·I:'·~e.~·]lt!~f:o~$~~;:~rn) Fuellriput Heat content .•.•••.Stealn.·i·········I. Gr~ss '.}leat Input.

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. Operating Data for Furnace and Air Pollution Control Equipment:

1. Were the fumace(s) and control equipment operated consistent with normal procedures? YES

2. Date(s) and procedure(s) oflast maintenance/cleaning within 6 months: February 19 - March 16,2007

3. Include a copy of chart/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 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 of APe 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, and Multi-clone: ~p (in. w.c.)

• Catalytic Incinerator :(OFinlet ,OFoutlet) and Thermal Incinerator: (OF oneratin.) • ESP: Numberand identity of operating field(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.-british thermal units gpm.-gallons per minute in.w.c.-inches of watercolumn

lbs.-pounds MW-megawatts psig-pressure persquareinchgauge AI'- pressure drop

Page 2 of3
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: Numberand identity of operating field(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 Water Flow 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 pollution control Btu.-british thermal units gpm-gallons per minute in. w.c.-inches of watercolumn

Ibs.-pounds MW-megawatts psig-pressure per 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: Thisform provides only a summary ofthe operating conditions during the performance test. Additional and more detailed

records are required to meet the requirements ofMinn. R. 7017.2035. Thisform is to be submitted as part ofthe performance test report.

aq-f6-ST04

Page 3 of3

Form ST-04,Page 1 of 1
Mlnnesotf

Pollution

Control

Agency

Operating Data Summary For CombustionSources

Minnesota Pollution.ControlAgency

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

Form ST-04

6/9/06

Test Date(s): May 3 & 7-8, 2007

Company Name: Hibbing Taconite 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, if applicable. LIST APPROPRIATE UNITS.

Run~& ... I·..Fuel Type & Ori~in FllelInPllt Heat content: . "<§tearn 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. Operating Data for Furnace and Air Pollution Control Equipment:

1. Were the fumace(s) and control equipment operated consistent with 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 of chart/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 soot blowing 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 of APe equipment and parameters 2:enerally monitored. Monitor as in the test plan 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

• Catalytic Incinerator :(OFinlet, °Foullet) and Thermal Incinerator: (OF oDeratin.) I • ESP: Numberand identity of operating field(s)

APC equipment and 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.-british thermal 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 of scrubber): 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 Water Flow Rate Maximum (gpm) 724 705 703 711

SV029 Water Flow Rate Minimum (gpm) 663 679 672 671

SV029 Water Flow Rate Average (gpm) 690 693 687 690

SV030 Water Flow Rate Maximum (gpm) 743 743 747 744

SV030 Water Flow Rate Minimum (gpm) 709 725 720 718

SV030 Water Flow Rate Average (gpm) 724 733 737 731

SV031 Water Flow Rate Maximum (gpm) 676 688 693 686

SV031 Water Flow Rate Minimum (gpm) 649 663 648 653

SV031 Water Flow Rate Average (gpm) 661 675 666 667

SV032 Water Flow Rate Maximum (gpm) 520 525 520 522

SV032 Water Flow Rate Minimum (gpm) 509 503 501 504

SV032 Water Flow Rate Average (gpm) 515 516 509 513

Abbreviations: APe-air pollution 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 ofthe operating conditions during the performance test. Additional and more detailed

records are required to meet the requirements ofMinn. R. 7017.2035. This form is to be submitted as part ofthe 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

USEPA Method 2

Leak-Free Connections

Gas Flow

Flexible Tubing

0.64 em

(0.25 in) T Temperature Sensor IIE--E7.62 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. NOx

2. O2

3. CO2

4. CO

5. SO 2

n a

Exhaust

Data Recorder

Flow Control

Gas Analyzer

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 Molecular Weight

Md=

Wet Molecular Weight

0.5 20.0 79.5

Ms = Md x (l-Bws) + (18.0 x Bws)

Md =

Ms=

28.88 Bws = 0.06

Meter Volume 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 of Water Vapor Condensed

Vwc(std) =

33.6

Vwc(std) =

3S
Example Calculations

Page 2 of 3

Moisture Content

Bws = Vwc(std)

(Vwc(std)+Vm(std))

1.583 Vm(std) = 24.553 ----- ------ Vwc(std) =

Bws=

Average Duct Velocity

Vs = 85.49 x Cp x Sqrt ~p (avg) x (Ts (avg)/ (Ps x MS)Y1 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 =

Gas Emission 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

Cgas(dry)= 105.3 ----- Mwgas = 46.01

Ib/hr = 119.84

37
Customer:

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

ISpan Value: 413

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

39
Date:

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/RB

Start- 6:00 End- 6:30

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

40
Date:

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/RB

Start- 7:50 End- 8:20

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

4:1
Date:

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

42
Customer:

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

44
PITOT 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

45
Date:

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/RB

Start- 8:15 End- 8:25

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

46
PITOT 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 (H20 U) :

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

Rectangular Duct: 0.00

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

47
Customer:

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

49
Date:

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

50
Date:

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

51
Date:

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

52
Customer:

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

54
PITOT 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

S5
Date:

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

56
Date:

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

57
Customer:

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

59
Date:

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

60
Date:

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): •.••••....••••.•.•..•. 158258
Date:

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

62
Customer:

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

64
Date:

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

65
Date:

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

66
Date:

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

67
Customer:

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

69
Date:

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

70
Date:

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

72
Customer:

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

74
Date:

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

75
Date,

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

76
Date:

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

77
Customer:

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

79
Date:

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

80
Date:

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

81
Date:

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 c

O• 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

82
Customer:

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

84
Date:

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

85
Date:

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

86
Date:

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

87
Customer:

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

89
Date:

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

i

115

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

90
Date:

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 (H20 n) :

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

92
Customer:

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

Ispan Value: 413

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

94
PITOT 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

95
Date:

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 (H20 n) :

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

96
Date:

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

97
SV021 SV021 SV021

Run1 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

98
SV022 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

99
SV023 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: 60
SV024 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: 60
SV026 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

:103
SV027 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: 60
SV028 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

205
SV029 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

:106
SV030 SV030 SV030

Run 1 Run

2 Run3

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: 60
SV031 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: 60
SV032 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 .5e-...m-« JYIJI) 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»

A1/'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~ J0, iJ'C' 'l/). 17

')'16" - ''1b /4:2.. .J::!i:;:t I. 7 ;,):J 3. '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, CO2OJ' 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

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 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;ySystem 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, qLf ~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, CO2 or NOx on Turbines.

Acceptable system response for 02, 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 02, CO2, 802 or NOx (non-turbine applications): ± 3% of span

Acceptable system drift for 02, CO2or 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,.""

JLf ~~ ... (.,'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 :l1.0 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.( n D 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

_.II Iv Port Point ~p ("H2O) Ts ('1-)

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: 1215

Post Test Leak Check: c::J~)...

Form 1012

Fail

CFM at _It-L....-_ "Hg

:145

GE Energy
Methods 2, 3 & 4 Field Data Sheet

Run Number: 3

Page L of L.

Date:

Pbar ("Hg):

r, 71" Pstatic ("H20):

Pitot ID:

Pitot Cp:

Meter ID:

Meter Y:

Meter t1H@i:

~'71 ' Operators:

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

, 'f J ~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'

Project#: I

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: - 11107

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):

}, oIJ)

Pitot ID:

Pitot Cp:

Meter ID:

MeterY:

Meter LiH@i:

4"1),/ Operators:

Project #:

Company:

Plant:

Source ID:

Load:

Stack Dim:

Stack Area:

Pre-Test Pitot Leak Check: Fail

I Time I Port I Point ILiP ("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 )JilJ C'~11 (-6 L Pitot 10: 00 f3 A

4,' h ~Q1J,& Pitot cp:

'#Jj,h-'~J/M1V Meter 10:

5 v0 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:

Stack Area:

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 o "7L ' La .... 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)

to>

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

Time Port

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: 'fr 2 I UPage .L of _I . Date:· S--I - D 7

Pbar ("Hg): .2 f. [ j

Pstatic ("H20 ): <. l' _---.-::.......-_- • 71 y;

rcr-,

r

Pitot 10:

Pitot Cp:

Meter fD:

MeterY:

Meter LlH@i:

o- 71 " Operators:

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;; JB 11 ..74 [os-:

l,i (1 B 12 ,,\C 't15

Use Bwsand 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~; 01

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-, JoJB 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 Bws and 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-- Ir;* - 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 "cn 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 Vm (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 ("H20 ):

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 JI Y

A 5 .d!Sr;-- II '-(

A 6 "q).-- )fll

A 7 ~g~ )t'-f

A 8 ,,~4 llL(

A 9 4>J1 II <..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{ '77 fl. ,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 II J----

B 7 ,,(Ie Ito

B 8 ~e~ /II

B 9 p~ II ').-'

B 10 .:7 f.:5 L/~

B 11 ,71 ill

B 12 ,(PO Joe

f7t lO

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: JiJl,.--

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~ /I L.(

,8 10 ..B)'- ilL{

8 11 .,70 1/ I

AQ..:1..:::::I

<t:;T J , 8 12 ,s-3 Jr:J f6

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 ("H20 ):

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: IrJ {

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» to 7

B 7 .7J /07

B 8 .67 107

B 9 , (C 1°7

B 10 .a: 16'6

B 11 ,td 16(

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 Vm (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

Pre-Test Leak Check: Pass 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

:;;;- 1,7/i Pstatic ("H20 ): _---:d.:..:-('L-5 _

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.77 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

i1.\ 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.e5Vo"/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 IPoint 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 Bwsand 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 ("H20 ): •_..L- f)~r _

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/ IlJ I:..f

tsro B 12 JJ g,/:' - -, _CJ.13,~,-:::::-...- . .

/02

[OZ

102

102

qq

/02

!D 2... (

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

I Lj 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 8Cf 5.,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~f1ife ~:~:~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

J10 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 to 2- '/~ '£) 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

I CJ 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 (Ocn-s- ",.

Total Train :L~HO .2.'1 i \~3

Bws: ---

% CO2:

Pre-Test Leak Check: CJ

Post Test Leak Check: •

Fail

CFM at I B 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 ("H20 ): _-_,~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)

Ts tF) II Time

'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

Time Port

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~

08'10 '\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 Bwsand MW data from previous Run? Yes No

Time Vm(fn Meter Meter Imp. Out llH

In (oF) Out (oF) (oF) ("H2O)

DUg IGte u 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 008A I'k~ b= 'R.e-:...l~ Pitot Cp:

rJ;:I,!.;\J Meter iD MeterY: 7~r_

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

Time Port

Pre-Test Pitot Leak Check: Pass Fail

Time Port Point .1.P ("H2O) Ts (oF)

'1 t.f 7 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 IQARII 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 o if .. 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 ("H20 ): - ..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.t fJ)

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: TWZ R

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 Port Point ~p ("H2O) Ts (oF) Time

1,/1(r{ A 1 ,,6 '10 rtf1J~) A 2 r~ <::to ./ v

A 3 ,)A (7 010

A 4 .. L <ltU

A 5 o '3 go

A 6 ,,(, n: '10

A 7 (

1: '3 qo

A 8 ,a , t{J

A 9 AI' 'J cIAJ

'A 10 c vt c . I/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 70J l-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):

Pitot ID: roBA

Pitot Cp:

Meter ID:

MeterY:

Meter ~H@i:

'0. ) I 7 Operators:

>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 ile. '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

lV

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

Mt L4.()3 'it Pitot ID:

HihbwCi_Ia conAte Pitot ce. Id(t/b.r~ Meter ID:

$YO b...5vMeter 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

f fI' 1

q8

0'

(.7

87

Time

1 r 1 If

1/232

I] l 3L

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 Bws and MW data from previous Run? Yes No

Time Meter

In tF)

Imp. Out L1H

(OF) ("H20)

1//5"" 9 9 IJ/~r;. 00

Ii 20 ') 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 _ fn "Hg

Form 1012

:168

GE Energy
Pitot ID: 008A 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.A6 34;;

Company: =mt:bjil)qTacDni!e

Plant:

Source ID: 3 vo L It

Load: 5reate,.. +.--hQ-n---:Cf::-O----::~::--:i:).------

Stack Dim:

Stack Area:

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 Bws and MW data from previous Run? Yes No

Time Port Point .L\P ("H2O) Ts (OF)

B 1 LJ 9) I D 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) ("H2O)

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: ,,00 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:

BMl;~-& ~o~ftE SIIO'Lt'j

Pitot 10: 008 A

Pifot Cp:

Meter 10: :3 67 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 ("H20 ):

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

IPoint I

fA It'

f41'2

/4/')

Time Port Point LlP ("H2O) Ts I Time I Port (OF)

141(" A ( ,7~ q7

V, ~f~) 2 .,qR 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 tt\ 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: 6'815 0

Meter Y: I,' <r

Meter ~H@i: 1, 7 If3

Operators: T WI R g (

Run Number: J /

Page .L of f

Date: - )',.7·tn

Pbar ("Hg): --=~~.{'-----__

Pstatic ("H20 ): _---=()'--,,"--__

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 o ZB 10 '/ ID2.

B 11 ,QZ ,"02-

0820 B 12 ,84 Cfl

(7 ],oJ

Use Bwsand MW data 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 IV\ "Hg

Form 1012 GE Energy
Run Number: -;f:. ;<-.

Page f of I

Date: - - 5-8- 0 7

Pbar ("Hg): _2--'-,0':",-6-:--__ Pstatic ("H20 ): - ti, g

Pitot ID: 008 A

Pitot Cp:

Meter ID: 88750

MeterY: 1.1"( Meter~H@i: r-B

'"6- 7 ( Operators: T =Z R.f?

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 Bws and 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 ("H20 ) Ts (oF)

th "-I~' A 1 ,,7/ I Ol-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 _ I i1 "Hg

Form 1012 GE Energy
-0.75

Run Number:

Page _,_ of _1_

Date:

Pbar ("Hg):

t. 7/'} Pstatic ("H20 ):

Pitot ID: 008/1

Pitot Cp:

Meter ID:

MeterY:

Meter ~H@i:

/6.7/ ' Operators:

I CfIJj·

'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 MW data from previous Run? Yes No

Time Vm (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 ") 7vft.!

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, () ItIf

B 8 I. C> 1/'1

B 9 ().~O / / 'I

B 10 P. Ii 1. /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 ("H20 ): _-_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 IUB 10 . "51 fld-.

B 11 . 1'0 r(lO? 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( b2 /. i;

4 (.1 7..6 C'fl. ,-

Total Train

Bws:---

176

Pre-Test Leak Check: Pass 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~ Meter Y:

). 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 ws and 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 r 41 /~3

B 6 I I jty3

B 7 ,Ie'7 / )--';>

B 8 Jlep7 /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 Vm (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: Iij. '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 ("H20 ): _---"--'(;..'-"~'__ __

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 I Z (

A 4 /,; j 2/

A 5 1,2- (2 )

A 6 I .. I / Z J

A 7 I 4' 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 JJ1 / /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 Bwsand MW data from previous Run? Yes No

Imp#

Total Train

Initial Final Net

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

ot so /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 Energy
Control Module No.

Standard Meter No.

Standard Meter (Yr)

38758

13124821

0.994

Pre Test DGM 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

Outlet Temp. 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. Calibration Before Use. Pre Test Calibration 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 ...... -..

II Scott Speclalty 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)

First Tnad 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:~ - -..

:183
AftJ.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 01May2008

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 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

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 (GEInfra, Energy); Beresford, Robert

Subject: Test Plan Approval

Page I of I

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 order to 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,

Andy Place

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 exclusive use ofthe individual or

entity to which it is intended to be addressed. This message may contain information that is privileged or confidential

and thereby exempt and protected from unauthorized disclosure under applicable law. Ifthe reader ofthis message is

not the intended recipient, or an employee or agent responsible for delivering the message to 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. If you 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): Pellet Indurating Furnace Stacks (GP003/SV021-SV032) for BART analysis and Line I Furnace

Stack (SV021-SV024) for NOx variablity

Scheduled For: April 30, 2007, at your Facility located in Hibbing, Minnesota.

Your test plan submitted on April 30, 2007, and discussed on May 1,2007, has been approved

by the Minnesota Pollution Control Agency (MPCA) as follows:

D Shortened test notification approved

IZI Test plan approved without modification

D Test plan approved with the following provisions:

Include greenball feedrate (feed to grate), fired pellet production rate, and time of operation

during test. Rates can be summarized in "per hour" measurements with supporting data

included in test report.

Include Facility Name, AQ File No., Source Designator as listed in permit (EUOOO, SVOOO,

GPOOO, etc.), and Test Date on the face ofthe CD copy.

Please complete Performance Test Report Completeness Criteria checklist to ensure all

required information is included in the report and in proper 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- Asphalt Plants

Microfiche/CD-ROM Submittal Form

IZI Operating Data Summary- Combustion

Sources

IZI Operating Data Summary- Process Sources D

IZI Certifications Form IZI

IZI Performance Test Report Completeness 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 if you have any questions regarding this approval.

1.89
Please be aware that enforcement action will be taken for performance test failures indicating emissions above applicable limits

(excess actual emissions to the environment). Failures commonly result in assessment ofa monetary penalty. Upon the first test

failure, the Company should take immediate measures to minimize emissions. The measures taken should be documented, as

they will become part ofthe record ofcorrective actions.

Hard Copy Performance Test Reports and Microfiche or CD Copy submittals will be addressed to: Compliance Tracking

Coordinator, Compliance and Enforcement Unit, Industrial Division, 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 Straight Grate Pelletizing Furnace Test for NOx

Part I: General Information

1. Name and address of emission facility:

Hibbing Taconite Company

Highway 5 North

P.O. Box 589

Hibbing, MN 55746

2. Emission facility contact person:

Andrea 1. Hayden

Section Manager - Environmental

Phone: (218) 262-6856

Fax: (218) 262-6877

3. Permit Number / AQD File Number:

13700061-002

4. Purpose for performance testing:

a. To quantify NOx emissions for use in the 2007-2011 Air Emission Inventories.

b. To provide quantitative data for BART Analysis regarding potential NOx reductions due to three

Energy and Emission Reduction Projects (Combustion Chamber Upper Air Inlet Modifications)

performed at Hibbing Taconite Company on Furnace Lines 1, 2 and 3 during 2005 and 2006.

5. Schematic drawing ofstack and sample ports:

See Appendix A

6. Location of plant:

Hibbing Taconite Company

2 miles West ofHwy 5 N

Hibbing, MN 55746

7. Contracted testing company information:

GE Energy Management Services, Inc.

1301 Corporate Center Drive - Suite 177 Eagan, MN 55121

Contact: Bruce Randall, MN Regional Manager

Phone: (651) 686-0700, extension 16

Fax: (651) 686-4434

191.

Page 1 of 4
Part II. Testing Requirements

1. The following is a description of each pollutant to be tested, the applicable emission limits, and the applicable rule or regulation for each emission

limit:

EU#! Process Pollutant EmissionLimit Applicable Rule 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 sampling procedure 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 of Federal Regulation, Title

40 Part 60, Appendix A, Method 19 - Table 19-2.

Part III. Operating Conditions

1. Processes to be tested and control equipment monitored: L L

EU#! ProcessEquipment Maximum .....ControlEquipment Control'Equipment Operating Parameters during Fuel ...

SV# Description Design Capacity Description Testing and how Monitored and Recorded Burned

430 dry short Venturi wet Venturi scrubbers - average of continuous pressure Natural

EU 020-022 Pellet Indurating tons of pellets scrubber! drop readings across the venturi and demist panels, 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 information will be recorded during the test and submitted with the test report:

A. Processing rate and total amount of product made during each run (by weight).

B. Amount and type ofraw material used during each run (by weight).

C. Amount of natural gas used during each run (by volume) (indurating furnace only).

D. Dust collector operating parameters.

E. Description and date of last maintenance work done before the test.

F. Record keeping of operational parameters as measured during the test.

G. Calculations.

H. Certification ofthe data by a responsible party.

2. Explanation of why the proposed test conditions are considered to be worst case in accordance with MN Rule 7017.2025, Subp. 2:

For all emissions units, testing will be performed while the units operate at practical maximum capacity as conditions allow

during the test period.

Part IV. Test Methods

1. Listed below in Section 2 are the methods to be used for this test.

2. The following is a description ofthe number oftest runs, length oftest runs, and sampling rate for each pollutant.

C.D

W

A. EPA Method 1 for location ofsampling ports and location oftraverse points. A single run ofthis method will be performed to determine

traverse point locations and evaluate cyclonic flow conditions at each emission point prior to the performance ofthe remaining test

methods.

B. EPA Method 2 for duct velocity and volumetric flow rate. Three determinations: one measurement concurrently with each test run for NOx

at each emission point.

C. EPA Method 3 for fixed gas analysis on combustion sources. One test run on an integrated sample collected concurrently with each test run

for NOx at each emission point.

D. EPA Method 4 for the determination of moisture in the flue gas. One test run concurrently with each test run for NOx at each emission

point. Approximate sample rate of 0.75 CFM, approximate sample time of30 minutes.

E. EPA Method 7E for NOx. Three sample runs will be conducted with a sample time of 60 minutes at each emission point.

Page 3 of4
v. Other

1. Gaseous pollutants, in this case NOx, will be reported in terms of concentrations (PPMdry) and emission rate (#/MMBtu & #/hr).

2. Test schedule: See Attachment B.

...

r..D

Page 4 of 4
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