COMPLIANCE TEST REPORT

BAGHOUSE NO. 5

AT

NOVELIS, INC. PROJECT ID: KR-7102

PREPARED FOR:

NOVELIS, INC. 1261 WILLOW RUN ROAD

GREENSBORO, GEORGIA 30642

PREPARED BY:

ADVANCED INDUSTRIAL RESOURCES, INC. 3407 NOVIS POINTE

ACWORTH, GEORGIA 30101

FEBRUARY 22-23, 2012

ADVANCED INDUSTRIAL RESOURCES, INC.

3407 NOVIS POINTE ACWORTH, GEORGIA 30101 V. 404.843.2100 F. 404.845.0020

ADVANCED INDUSTRIAL RESOURCES, INC.

3407 NOVIS POINTE ACWORTH, GEORGIA 30101 V. 404.843.2100 F. 404.845.0020
ADVANCED INDUSTRIAL RESOURCES, INC.

3407 NOVIS POINTE ACWORTH, GEORGIA 30101 V. 404.843.2100 F. 404.845.0020
TABLE OF CONTENTS

1.0 INTRODUCTION 1

1.1 SUMMARY OF TEST PROGRAM 1

1.2 KEY PERSONNEL 2

2.0 PLANT AND SAMPLING LOCATION DESCRIPTIONS 3

2.1 PROCESS & CONTROL EQUIPMENT DESCRIPTION 3

2.2 MACT PROCESSES AND STANDARDS 3

2.3 RAW MATERIALS 4

2.4 CYCLE TIMES 4

2.5 PROCESS MONITORING 5

2.6 SAMPLING LOCATION 5

3.0 SUMMARY AND DISCUSSION OF TEST RESULTS 6

3.1 OBJECTIVES 6

3.2 FIELD TEST CHANGES AND PROBLEMS 6

3.3 PRESENTATION OF TEST RESULTS 6

3.4 PROCESS MONITORING 8

4.0 SAMPLING AND ANALYTICAL PROCEDURES 9

5.0 INTERNAL QUALITY ASSURANCE ACTIVITIES 10

5.1 INTERNAL QUALITY ASSURANCE 10

5.2 SAMPLING TRAIN LEAK CHECKS 10

5.3 PROBE NOZZLE DIAMETER CHECKS 11

5.4 PITOT TUBE FACE PLANE ALIGNMENT CHECK 11

5.5 METERING SYSTEM CALIBRATION 11

5.6 TEMPERATURE GAUGE CALIBRATION 12

5.7 SAMPLE HANDLING AND CHAIN OF CUSTODY PROCEDURES 12

5.8 DATA REDUCTION CHECKS 12

5.9 EXTERNAL QUALITY ASSURANCE 13

5.9.1 TEST PROTOCOL EVALUATION 13

5.9.2 ON-SITE TEST EVALUATION 13

6.0 DATA QUALITY OBJECTIVES 14

LIST OF APPENDICES

APPENDIX A TEST RESULTS

APPENDIX B FIELD DATA REDUCTION

APPENDIX C EXAMPLE CALCULATIONS AND NOMENCLATURE

APPENDIX D FIELD DATA

APPENDIX E LABORATORY REPORT

APPENDIX F CALIBRATION DATA

APPENDIX G PROCESS OPERATION DATA
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

Compliance Test Report- BAG5 Page 1 of 14

Advanced Industrial Resources, Inc.

1.0 INTRODUCTION

1.1 SUMMARY OF TEST PROGRAM

Novelis, Inc. (Novelis) operates a Secondary Aluminum production facility in

Greensboro, Georgia. The facility is subject to the Georgia Environmental Protection

Division (EPD) Title V Operating Permit No. 3341-133-0001-V-03-0 and the Maximum

Achievable Control Technology (MACT) requirements of Title 40 of the Code of Federal

Regulations, Part 63 (40 CFR 63) Subpart RRR (Secondary Aluminum MACT).

The Baghouse 5 (BAG5) exhaust was previously tested on December 15-16, 2011 to

determine the filterable particulate matter (PM), dioxins/furans (D/F), and hydrogen

chloride (HCl) emission rates and concentrations for compliance demonstration purposes.

PM and D/F emissions during the 2011 compliance demonstration were found to be well

below the established emission limits. However, the HCl emissions were found to be

exceeding the applicable emission limits on the day of testing. Therefore, the test

program described in this report was conducted as a re-test to provide data and

demonstrate that the BAG5 HCl emissions meet the applicable emissions limitations.

The test program was conducted in accordance with a Georgia EPD-approved Site- Specific Test Protocol (SSTP) to document that this source operates below the applicable

emissions limits in 40 CFR 63.1505 and the facility’s Title V Permit 3341-133-0001-V- 03-0. The field sampling portion of the test program was conducted February 22-23, 2012. All

field sampling and reporting activities were conducted by Advanced Industrial

Resources, Inc. (AIR). This Test Report presents the results of the compliance test

program.
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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1.2 KEY PERSONNEL

The key personnel responsible for the coordination and performance of test program

activities are:

Allan Dean, Novelis, Inc. (706) 454-3210

Robert Higdon, Novelis, Inc. (706) 454-3235

Derek Stephens, Advanced Industrial Resources (404) 843-2100

Scott Wilson, Advanced Industrial Resources 800-224-5007
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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Advanced Industrial Resources, Inc.

2.0 PLANT AND SAMPLING LOCATION DESCRIPTIONS

2.1 PROCESS & CONTROL EQUIPMENT DESCRIPTION

Novelis operates a secondary aluminum production facility in Greensboro, Georgia.

Novelis recycles used beverage cans (UBC) and scrap aluminum into large stock ingots

that are shipped to rolling mills where they are rolled into coils of beverage can sheet

stock. Baled aluminum cans are broken up and fed into a shredder (source code SHRD)

reducing the aluminum to one-half to one-inch sized pieces. Iron and steel are removed

with a magnetic separator and dirt is separated out using screens. Shredded aluminum is

fed into a decoater (source code DCTR), which uses hot air to remove paint and lacquer.

The decoater exhaust is vented back to the decoater for heat recovery. The aluminum is

then fed into one of three reverberatory melt furnaces (source codes FCE1, FCE2, and

FCE3). The furnaces are fired with either natural gas or propane. Dross removal occurs

at the furnaces. Molten metal is gravity fed to a natural gas or propane fired holding

furnace (source code HOLD) for metal cleaning and transfer to the casting unit. A

mixture of chlorine and argon gases is injected in-line to remove impurities from the

molten aluminum. Excess gas is removed in a compact degasser. A direct chill caster is

used to form aluminum ingots weighing 50,000 to 60,000 pounds each.

2.2 MACT PROCESSES AND STANDARDS

Of the processes at the facility, several are subject to the emission limits and monitoring

requirements of the Secondary Aluminum MACT and the prevention of significant

deterioration (PSD). These include the two shredders, a decoater, three melt furnaces,

two induction furnaces, ACD, and a holding furnace.

Each of the three reverberatory melt furnaces is classified as a Group 1 furnace under 40

CFR 63.1503 since coated aluminum, at times, is melted in them. Emissions from the

side wells and main hearths on the No. 1 and No. 2 Melting Furnaces are controlled by

two lime-injected baghouses (BAG1 and BAG2), which discharge through a common

stack. Emissions from the side well on Furnace 3 are controlled by another lime-injected

baghouse (BAG5).
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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The holding furnace is classified as a Group 1 furnace since reactive flux is used to clean

and process the molten aluminum. The compact degasser is classified as an in-line

fluxer. Emissions from the in-line fluxer are ducted to the flame zone of the burner for

the holding furnace to achieve oxidation of any pollutants that may be present. The

exhaust from the holding furnace, which then includes exhaust from the in-line fluxer, is

discharged to the atmosphere through the holding furnace stack.

Collectively the four Group 1 furnaces and the in-line fluxer may be classified as a

secondary aluminum processing unit (SAPU). 40 CFR 63.1505(k) provides equations for

calculating SAPU emission limits based upon PM, HCl and D/F emission standards for

the individual emission sources, which are established in 40 CFR 63.1505(i) and (j). The

equations are based upon charge rates or may be based upon production rates, at the

discretion of Novelis, in accordance with 40 CFR 63.1506(d)(3). Emission rates were

calculated based upon output production rate. Charge and production rate data is

presented in Appendix G.

2.3 RAW MATERIALS

UBC and scrap aluminum are transported to the facility by rail car and truck. Coated

aluminum, including all UBC, is fed into the shredding and decoating processes. Coated

and uncoated scrap aluminum and alloys are fed directly into the three melt furnaces. .

While performance tests were being conducted, the furnaces were operated at optimal

production level with charge materials representative of the range of materials processed

by the unit and at the optimal reactive fluxing rate. Charge, production, and fluxing rate

data are presented in Appendix G.

2.4 CYCLE TIMES

The facility includes batch processes in the melt furnaces. Each test run was conducted

for the period of the source’s entire process operating cycle. Cycle times for this period

ranged from approximately 6.0 to 7.0 hours.
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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Advanced Industrial Resources, Inc.

2.5 PROCESS MONITORING

All essential process monitoring equipment on the emission sources and control

equipment were operating properly and recording data throughout the test period so as to

allow necessary monitoring parameters and limits to be established. Monitoring data is

presented in Appendix G.

2.6 SAMPLING LOCATION

The BAG5 sampling point is located 3.1 equivalent stack diameters downstream from the

nearest upstream flow disturbance and 1.4 equivalent stack diameters upstream from the

stack exhaust. The duct has a circular cross-section with an internal diameter of 59.0

inches. The stack has two sampling ports oriented 90 degrees to one another in a plane

perpendicular to the exhaust gas flow direction. A schematic diagram of the sampling

location is presented in Appendix D. Twenty four sampling points (twelve traverse

points in each of the two sampling ports) were used for USEPA Methods 2, 3, 4 and 26A

sampling, in accordance with the requirements of USEPA Method 1.
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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Advanced Industrial Resources, Inc.

3.0 SUMMARY AND DISCUSSION OF TEST RESULTS

3.1 OBJECTIVES

Novelis, Inc. operates a Secondary Aluminum production facility in Greensboro,

Georgia. The facility is subject to the Maximum Achievable Control Technology

(MACT) requirements of Title 40 of the Code of Federal Regulations, Part 63 (40 CFR

63) Subpart RRR (Secondary Aluminum MACT) and its Title V Permit 3341-133-0001- V-03-0. The Furnace 3 total emissions (sidewells and main hearth) were tested under a

single maximum throughput operating condition during three separate batch process

cycles to determine hydrogen chloride (HCl) emission rates.

3.2 FIELD TEST CHANGES AND PROBLEMS

The testing was conducted in accordance with the Site-Specific Test Protocol submitted

to Georgia EPD prior to testing. No significant problems were encountered during

testing that required deviation from the planned test protocol.

Due to varying lengths of the process cycle times, test durations varied from 6.0 to 7.0

hours. Traverse point sample durations utilized were 10 minutes per point and upon

sampling at the initial 24 traverse points, testing continued by starting back at the

respective traverse point 1 in the first port sampled, respectively.

3.3 PRESENTATION OF TEST RESULTS

Emission rates are summarized and compared to applicable MACT and permit limits in

Table 3-2. Table 3-1 contains the Performance Test Matrix data and Table 3-3

summarizes the Operating Parameter Values measured throughout the testing.

Concentrations and mass rates are presented in Appendix A. Reduced and tabulated data

from the field-testing is included in Appendix B. The calculations and nomenclature

used to reduce the data are presented in Appendix C. Actual raw field data sheets are

presented in Appendix D.
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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Table 3-1: Performance Test Matrix

Source Source

Code

Air

pollution

control

device

Stack

ID Analytes EPAMethods

Test run

duration

Run

Number Date

Start - Stop

Time

FCE3

side

well &

main

hearth

FCE3 BAG5 BAG5 HCl 1, 2, 3,

4, 26A

390 min

(6.5hrs) 1 2/22/2012 8:00- 14:40

420 min

(7 hrs) 2 2/22/2012 15:10- 20:20

360 min

(6.0 hrs) 3 2/23/2012 9:20- 15:30

Table 3-2: MACT Performance Test Results Summary for SAPU

Based on Production Output Rates (2/22-23/2012)

BAG3 / FCE3

Test 1 Test 2 Test 3 Average

EHCl lb/cycle 1.76 2.93 3.37 2.69

Ti ton

production/cycle 43.7 52.6 37.0 44.4

EHCl

lb/ton

production 0.0403 0.0558 0.0911 0.0624

EHCl, Allow

lb/ton

production 0.40 0.40 0.40 0.40

% of PM

allowable % 10% 14% 23% 16%
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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Table 3-3: Operating Parameter Values during Test

(newly established operating parameters)

Source or APC

Device Source Code

Source or

APC Name Operating Parameter (units) Limiting Value

FCE1, 2 & 3 Melt furnaces

1, 2 and 3

Average reactive flux injection

rate Production

FCE3 or BAG5 Baghouse 5

Inlet temperature (degrees F) 163

Production (tons / cycle) 44.4

Total Paint Coated Scrap (lbs /

cycle) 32,244

Average reactive flux injection

rate Total salt (total available

Chlorine) lbs / cycle)

2314 (1194)

Lime feed conveyor speed (Hz) 12

3.4 PROCESS MONITORING

All essential process monitoring equipment on the process at Novelis were operating

properly and recording data throughout the test period so as to allow necessary

monitoring parameters and limits to be established. Data is presented in Appendix G.
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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Advanced Industrial Resources, Inc.

4.0 SAMPLING AND ANALYTICAL PROCEDURES

The testing was conducted on in accordance with 40 CFR 60 Appendix A. Specifically:

 EPA Method 1 was used for the qualification of the location of sampling ports

and for the determination of the number and positions of stack traverse points, as

applicable to sample traverses for Method 2.

 EPA Method 2 was employed for the determination of the stack gas velocity and

volumetric flow rate during stack sampling using the Type “S” Pitot tube.

 EPA Method 3 was used for the calculation of the density and dry molecular

weight of the effluent stack gas.

 EPA Method 4 was used for the determination of moisture content.

 EPA Method 26A was used for the determination of hydrogen chloride (HCl)

emission concentration and rates.

All samples were stored upright in a closed sample box until final laboratory analysis. In

order to limit the chain of custody, only essential AIR personnel were permitted access to

these samples.
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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Advanced Industrial Resources, Inc.

5.0 INTERNAL QUALITY ASSURANCE ACTIVITIES

The quality assurance/quality control (QA/QC) measures associated with the sampling

and analysis procedures given in the noted EPA reference methodologies, in Subparts A

of 40 CFR 60 and 40 CFR 63, and in the EPA QA/QC Handbook, Volume III (EPA

600/R-94/038c) were employed, as applicable. Such measures included, but were not

limited to, the procedures detailed below.

5.1 INTERNAL QUALITY ASSURANCE

The quality assurance/quality control (QA/QC) measures associated with the sampling

and analysis procedures given in the noted EPA reference methodologies, in Subparts A

of 40 CFR 60 and 40 CFR 63, and in the EPA QA/QC Handbook, Volume III (EPA

600/R-94/038c) were employed, as applicable. Such measures include, but are not

limited to, the procedures detailed below.

5.2 SAMPLING TRAIN LEAK CHECKS

Determinations of the leakage rate of the Method 5 type sampling trains were made

before and after each sampling run using the procedure detailed in Section 8.1.4 of EPA

Method 5. Before the sampling run, after the sampling trains had been assembled and

probe and filter box temperatures had time enough to settle at their appropriate operating

values, the probe nozzle was plugged and the system was evacuated to a pressure of 15

inches of Hg below ambient pressure. The volumetric leakage rate was measured by the

dry gas meter over the course of one (1) minute. The leakage rate was less than 0.020

cfm for each run, thereby meeting the maximum allowable leakage rate.

After the sampling run, before the train was disassembled the probe nozzle was plugged

and the system depressurized to a vacuum equal to or greater than the maximum value

reached during the sampling run. The dry gas meter measured the volumetric leakage

rate over the course of one (1) minute. Except as noted in Section 3.2 of this report, the

leakage rate was determined to be less than 0.020 cfm, thereby meeting the maximum

allowable leakage rate.
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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The Type “S” Pitot tube assembly was also checked for leaks before and after sampling

runs using the procedure in Section 8.1 of EPA Method 2. The impact opening of the

Pitot tube was blown through until a pressure of at least 3 inches of water registered on

the manometer. The impact opening was quickly plugged and held for at least 15

seconds, during which time the manometer reading held. The same operation was

performed on the static pressure side of the Pitot tube, except suction was used to obtain

the pressure differential.

5.3 PROBE NOZZLE DIAMETER CHECKS

Probe nozzles were calibrated before field testing by measuring the internal diameter of

the nozzle entrance orifice along three different diameters. Each diameter was measured

to the nearest 0.001 inch, and all measurements were averaged. The diameters were

within the limit of acceptable variation of 0.004”.

5.4 PITOT TUBE FACE PLANE ALIGNMENT CHECK

Before field testing, each Type S Pitot tube was examined in order to verify that the face

planes of the tube were properly aligned, per Method 2 of 40 CFR 60, Appendix A. The

external tubing diameter and base-to-face plane distances were measured in order to

verify the use of 0.84 as the baseline (isolated) Pitot coefficient. At that time the entire

probe assembly (i.e., the sampling probe, nozzle, thermocouple, and Pitot tube) was

inspected in order to verify that its components met the interference-free alignment

specifications given in EPA Method 2. Because the specifications were met, then the

baseline Pitot coefficient was used for the entire probe assembly.

After field testing, the face plane alignment of each Pitot tube was checked. No damage

to the tube orifices was noted.

5.5 METERING SYSTEM CALIBRATION

Every three months each dry gas meter (DGM) console is calibrated at five orifice

settings according to Method 5 of 40 CFR 60, Appendix A. From the calibration data,

calculations of the values of Ym and H@ are made, and an average of each set of values
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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is obtained. The limit of total variation of Ym values is +0.02, and the limit for H@

values is +0.20.

After field testing, the calibration of the DGM console was checked by performing three

calibration runs at a single intermediate orifice setting that is representative of the range

used during field-testing. Each DGM was within the limit of acceptable relative variation

from Ym of 5.0%.

5.6 TEMPERATURE GAUGE CALIBRATION

After field testing, the temperature measuring instruments on each sampling train was

calibrated against standardized mercury-in-glass reference thermometers. Each indicated

temperature was within the limit of acceptable variation between the absolute reference

temperature and the absolute indicated temperature of 1.5%.

5.7 SAMPLE HANDLING AND CHAIN OF CUSTODY PROCEDURES

All samples were transported in a closed sample box, the security of which was the

responsibility of the AIR Test Director, Mr. Mark Eddy. These samples were received,

checked, and numbered by the Test Director and custody records were written. The AIR

QA Director, Mr. Derek Stephens, then again checked the integrity of the samples and

their identification.

The samples collected during the test program were placed in shipping coolers with

sufficient insulation to prevent breakage during shipping. All samples in a shipping

container were listed on the chain-of-custody form enclosed in the shipping container.

Once the samples were securely packaged, the container was sealed with tape and several

custody seals were placed over the top edge so that the container could not be opened

without breaking the custody seals.

5.8 DATA REDUCTION CHECKS

AIR ran an independent check (using a validated computer program) of the calculations

with predetermined data before the field test, and the AIR Team Leader conducted spot
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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checks on-site to assure that data was being recorded accurately. After the test, AIR

checked the data input to assure that the raw data had been transferred to the computer

accurately. Flow rates, temperatures and moisture levels were relatively constant

(variation <5%) during the three test runs, which indicates that data recording and Method

2 and 4 sampling and calculation errors are not likely.

5.9 EXTERNAL QUALITY ASSURANCE

5.9.1 TEST PROTOCOL EVALUATION

A Site-Specific Test Protocol was submitted to the Georgia EPD in advance of testing,

which provided regulatory personnel the opportunity to review and comment upon the

test and quality assurance procedures used in conducting this testing.

5.9.2 ON-SITE TEST EVALUATION

A test schedule was submitted with the Site-Specific Test Protocol and Georgia EPD

personnel were notified of all changes in the schedule. No tests were performed earlier

than stated in the original schedule. Therefore, regulatory personnel were afforded the

opportunity for on-site evaluation of all test procedures.
Novelis, Inc. Greensboro, Georgia February 22-23, 2012

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Advanced Industrial Resources, Inc.

6.0 DATA QUALITY OBJECTIVES

The data quality objectives (DQOs) process is generally a seven-step iterative planning

approach to ensure development of sampling designs for data collection activities that

support decision making. The seven steps are as follows: (1) defining the problem; (2)

stating decisions and alternative actions; (3) identifying inputs into the decision; (4)

defining the study boundaries; (5) defining statistical parameters, specifying action levels,

and developing action logic; (6) specifying acceptable error limits; and (7) selecting

resource-effective sampling and analysis plan to meet the performance criteria. The first

five steps are primarily focused on identifying qualitative criteria such as the type of data

needed and defining how the data will be used. The sixth step defines quantitative

criteria and the seventh step is used to develop a data collection design. In regards to

emissions sampling, these steps have already been identified for typical monitoring

parameters.

Monitoring methods presented in 40 CFR 60 Appendix A indicate the following

regarding DQOs: Adherence to the requirements of this method will enhance the quality

of the data obtained from air pollutant sampling methods. At a minimum, each method

provides the following types of information: summary of method; equipment and

supplies; reagents and standards; sample collection, preservation, storage, and

transportation; quality control; calibration and standardization; analytical procedures,

data analysis and calculations; and alternative procedures. These test methods have been

designed and tested according to DQOs for emissions testing and analysis. These test

methods have been specified and were followed in accordance with the Test Protocol

submitted to Georgia EPD to ensure that DQOs were met for this project.
APPENDIX A

TEST RESULTS
Notes:

1) Allowable HCl emission limit from 40 CFR 63.1505(i)4 - 0.40 lb HCl/ton feed

*Process feed rate based upon production output

Pm

Pressure of meter gases

Ps Pressure of stack gases

Vm(std) Volume of gas sample

Vw(std),meas Meas. volume of water vapor

Bws,meas Measured moisture

Bws,theo Theoretical max. moisture

Bws,act Actual moisture

Md Mol. Wt. Of gas at DGM

Ms Mol. Wt. Of gas at stack

vs Velocity of stack gas

An Area of nozzle

0.015

28.85

0.245

0.000341

lb./lb.-mole

ft./sec 51.04

18.99

28.86

29.76

4.24

0.224

0.012

6.67

0.189 0.322

0.011

0.021

Novelis

Run 3

End Time 14:40

Average

22-Feb-12

Run 1 Run 2

9:20

23-Feb-12

5.10

317.26

4.38

15:10

Baghouse No. 5

Greensboro, Georgia

inches Hg 29.79

22-Feb-12

Units

30.06

scf

dscf 348.99

22:20

29.81

30.09

15:30

28.86

0.011

28.73

0.000341

HCl Test Results

Test Date

384.75

8:00

30.10

Start Time

ft2

51.66

ft2

0.000341

49.43

18.99

0.015

18.99

0.000341

18.99

28.61 28.70

50.71

28.84

lb./lb.-mole

0.012

0.021

inches Hg

344.95

dimensionless

28.74

29.81

30.11

Advanced Industrial Resources, Inc.

An Area of nozzle

As Area of stack

Gas Stream Flow Rates

Qa Vol. Flow rate of actual gas

Qsd Vol. Flow rate of dry gas

I Isokinetic sampling ratio

Process Data

Gas Stream Hydrogen Chloride Concentrations Method 26a

cHCl Conc. Of HCl in dry stack gas

cHCl Conc. Of HCl in dry stack gas

Hydrogen Chloride Mass Rates Method 26a

EHCl Emission rate of HCl

EHCl Emission rate of HCl

EHCl All1 Allowable HCl Emission Rate

% of All % of Allowable

57,768

44.4

0.0624

0.407

0.000341

16%

2.21

0.000965

6.63

100.8

0.4

23%

0.4

0.0911

0.547

0.0403

0.264

0.00132

mg/dscm 1.44 2.16

0.000943

3.02

lb/hour

6.00

37.0

50,596 48,250

99.7

48,904

percent 100.8

58,142

18.99

ft 0.000341 2

58,853

dscfm

ft2

0.000341

cfm 56,308

18.99

101.8

18.99

49,250

0.000341

18.99

7.34

14%

0.4 0.4

gr/dscf 0.000630

% 10%

lb/ton prod'n 0.0558

52.6

lb/ton prod'n

0.409

P (ouput) Feed Rate (output) tons/cycle 43.7

tons/hour 6.55
APPENDIX B

FIELD DATA REDUCTION
Vm

Volume of gas sample

Mlc Mass of liquid collected

p Velocity head of stack gas

( p)1/2 Square root of velocity head

H Pressure differential

Total sampling time

p Total production time

dcf

g

inches H2O

2.91

(inches H2O)1/2

minutes

366.816

420.0

3.04

0.250

inches H2O

minutes

End Time

Units

Cp:

22:20

Test Team: WLN, CS, RD

EPA Methods: 1, 2, 3A, 4, 26A

Console ID:

Ym:

Test Date

0.84

Novelis

Run 3

0.833

Client:

Location:

Source:

Greensboro, Georgia

Baghouse No. 5

C-008

0.954

H@: 1.973

Advanced Industrial Resources, Inc.

0.778 0.751

8:00

14:40

Data Reduction Sheet

15:30

Start Time 9:20

inches 0.250

HCl

Run 2

Analyte(s):

Run 1

400.0 430.0

89.8

0.856

390.0

0.733

141.4

15:10

92.9

414.884 345.933

0.824

2.93

360.0

22-Feb-12 22-Feb-12 23-Feb-12

0.250

370.0

Total sampling time

p Total production time

Dn Diameter of nozzle

Ds Diameter of stack

Tm

Temperature of meter

Ts Temperature of stack gas

Pbar Barometric pressure

pg Gauge pressure of stack gas

% O2 Percent O2 by volume

% CO2 Percent CO2 by volume

% N2 Percent N2 by volume

mHCl Hydrogen Chloride Mass

*Process feed rate based upon production output

minutes 420.0

605

inches

0.250

minutes

598

539

59.0

inches 0.250

546

400.0 430.0

390.0

59.0

360.0

6.0

27.168

73,989

37.0

0.250

620

59.0

552

0.00

370.0

percent (v/v) 20.80

°R

°R

inches Hg 29.89

inches H2O -1.10

14.098

79.1

23.516

29.89

79.0

20.80

0.20

-1.10

percent (v/v) 0.20

43.7

79.0

tons/cycle

percent (v/v)

mg

P(output) Feed Rate (output)

lb/cycle 87,388

tons/hour 6.6 7.3

105,162

52.6

-1.10

29.84

20.90
APPENDIX C

EXAMPLE CALCULATIONS

AND

NOMENCLATURE
Advanced Industrial Resources, Inc.

Sample Calculation Sheet

Novelis, Greensboro, Georgia

Baghouse No. 5, Run #1

Area of nozzle:

An = 3.1415 x Dn

2

 / 4 / 144 in

2

/ft2 An = 3.1415 x (0.25) / 4 / 144

An = 0.000341 ft2 Area of stack:

As = 3.1415 x Ds2

 / 4 / 144 in

2

/ft2 As = 3.1415 x (59) / 4 / 144

As = 18.99 ft2 Absolute pressure of meter gases:

Pm = Pbar + ∆H / 13.6

Pm = 29.89 + 2.908 /13.6

Pm = 30.10 inches Hg

Absolute pressure of stack gases:

Ps = Pbar + pg / 13.6

Ps = 29.89 + -1.1 / 13.6

Ps = 29.81 inches Hg

Volume of gas sample, standardized:

Vm(std)= Vm x Ym (Tstd / Tm) (Pm / Pstd)

*Note: Values may not agree exactly with results shown elsewhere in this report due strictly to rounding

Vm(std)= Vm x Ym (Tstd / Tm) (Pm / Pstd)

Vm(std)= (366.816) x (0.954) x (528/539) x (30.1/29.92)

Vm(std)= 344.86 dscf

Volume of water vapor in the gas sample, standardized:

Vw(std)= (Vlc x pw x R x Tstd) / (Mw x Pstd)

Vw(std)= (89.82) x (0.002201) x (21.85) x (528) / (18 x 29.92)

Vw(std)= 4.23 scf

Volume proportion of water in the stack gas stream, measured:

Bws,meas= Vw(std) / (Vm(std) + Vw(std))

Bws,meas= (4.23 / (344.86 + 4.23))

Bws,meas= 0.0121

Volume proportion of water in the stack gas stream, theoretical maximum:

Bws,theo= 10

{6.37-2827/(Ts - 95.2)}

 / Ps Bws,theo= 10 ^ {6.37-2827/(598 - 95.2)} / 29.81

Bws,theo= 0.1876

*Note: Values may not agree exactly with results shown elsewhere in this report due strictly to rounding
Advanced Industrial Resources, Inc.

Sample Calculation Sheet

Novelis, Greensboro, Georgia

Baghouse No. 5, Run #1

Volume proportion of water in the stack gas stream:

Bws,act= lower of Bws,meas and Bws,theo

Bws,act= 0.0121

Theoretical maximum moisture collection at saturation:

Vlc,theo= Vm(std) x Bws,theo / (1 - Bws,theo) / 0.04707

Vlc,theo= (344.86 x (0.1876) / (1 - 0.1876) / 0.04707

Vlc,theo= 1691.8

Nitrogen content of gas at the DGM:

%N2 = 100% - %CO2 - %O2 - %CO

%N2 = 100% - 0.2% - 20.8% - 0%

%N2 = 79 %

Molecular weight of gas at the DGM:

Md = ((44 x %CO2) + (32 x %O2) + (28 x (%N2 + %CO)))/100%

Md = ((44 x 0.2) + (32 x 20.8) + (28 (79 + 0)))/100%

Md = 28.86 lb/lb-mole

Molecular weight of gas at the stack:

Ms= Md (1 - Bws) + Mw x Bws Ms= (28.86 x (1 - 0.0121)) + (18 x 0.0121)

*Note: Values may not agree exactly with results shown elsewhere in this report due strictly to rounding

Ms= 28.73 lb/lb-mole

Velocity of stack gas: vs = Kp x Cp [∆p]1/2

 x [Ts/(PsMs)]1/2 vs = (85.49 x 0.84 x 0.824 x [598 / (29.81 x 28.73)]^1/2

vs = 49.45 ft/s

Volumetric flow rate of actual stack gas:

Qa = vs x As x 60 sec/min

Qa = (49.45) x (18.99) x (60 sec/min)

Qa = 56343 cfm

Volumetric flow rate of dry stack gas, standardized:

Qsd = (60 sec/min) x (1 - Bws) vs As (Tstd / Ts) x (Ps/Pstd)

Qsd = (60 sec/min) x (1 - 0.0121) x 49.45 x 18.99 x (528 / 598) x (29.81 / 29.92)

Qsd = 48965 dscfm

*Note: Values may not agree exactly with results shown elsewhere in this report due strictly to rounding
Advanced Industrial Resources, Inc.

Sample Calculation Sheet

Novelis, Greensboro, Georgia

Baghouse No. 5, Run #1

Isokinetic sampling ratio expressed as percentage:

I= 100 Ts [(K3 x Vlc)+ (Ym x Vm x Pm / Tm)] / ( 60 x Q x vs x Ps x An)

I=

I= 100.6 %

Concentration of HCl in dry stack gas, standardized: c= (m / Vm(std)) (35.32 ft3

 / m

3

) c= (14.098 / 344.86) x 35.32

c= 1.44 mg/dscm

Concentration of HCl in dry stack gas, standardized: c= (mg/dscm) / (35.32 ft3

 / m

3

) / (64.8 mg/gr) c= (1.44389) / 35.32 / 64.8

c= 0.000631 gr/dscf

Emission rate of HCl, time basis:

E= cmg/dscm x Qsd x (60 min/hr) x (2.2046 x 10

-6

 lb/mg) / (35.32 ft3 / m

3

)

E= 1.44389 x 48965 x 60 x 2.2046 x 10-6 / 35.32

E= 0.265 lb/hr

100 x (598) x ((0.002669 x 89.82) + (0.954 x 366.816 x 30.1 / 539)))/(60 x 390 x 49.45 x 29.81 x 0.000341)

*Note: Values may not agree exactly with results shown elsewhere in this report due strictly to rounding
EXAMPLE CALCULATIONS

An = Dn

2

 / 4

As = Ds2 / 4

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

canalyte = (manalyte / Vm(std)) (35.31466 ft3/m3)

‘canalyte = (manalyte / Vm(std)) (0.015432 gr/mg)

canalyte = ‘canalyte MWanalyte / 24.04 l/mol

CC = t0.975 (Sd / n1/2)

d = 1/n (Sdi)

DE = (EInlet – EOutlet) / E,Inlet x 100%

Eanalyte = (manalyte / Vm(std)) Qsd (60 min/hr) (2.2046x10-6lb./mg)

Eanalyte = canalyte Qsd (60 min/hr) (2.2046x10-6lb./mg)

I = 100 Ts (K3 Vlc + Ym Vm Pm / Tm) / (60  vs Ps An)

where K3 = 0.002669 (in. Hg ft3) / (mL R)

KI = [(2.0084x107 H@) An (1 – Bws)]2 (Md / Ms) (Tm / Ts) (Ps / Pm)

Md = 0.44 (% CO2) + 0.32 (% O2) + 0.28 (% N2 + % CO)

Ms = Md (1 – Bws) + Mw Bws P = Qsd / F-Factor x 60 x (20.9-O2) / 20.9

Pm = Pbar + H / 13.6

Ps = Pbar + pg / 13.6

Qa = (60 s/min) vs As Qsd = (60 s/min) (1 - Bws) vs As (Tstd / Ts) (Ps / Pstd)

RA = [Abs(d) + Abs(CC)]/RM

Sd = [(Sdi

2 – (Sdi)2

/n)/(n-1)]1/2

Tm = tm + 460 Ts = ts + 460 Vm(std) = Vm Ym (Tstd / Tm) (Pm / Pstd)

Vw(std) = (Vlc w R Tstd) / (Mw Pstd)

vs = Kp Cp [p]1/2 [Ts / (Ps Ms)]1/2
NOMENCLATURE

Symbol Units Description

Abs(x) dimensionless Absolute value of parameter x

An ft2 Area of the nozzle

As ft2 Area of the stack

Bws dimensionless Volume proportion of water in the stack gas stream

Cp dimensionless Type S pitot tube coefficient

canalyte mg/dscm Concentration of analyte in dry stack gas,

standardized

'canalyte gr./dscf Concentration of analyte in dry stack gas,

standardized

'canalyte ppm Concentration of analyte in dry stack gas,

standardized

CC dimensionless One-tailed 2.5% error confidence coefficient

d ppm Arithmetic mean of differences

di ppm Difference between individual CEM and reference

method concentration value

Dn inches Internal diameter of the nozzle at the entrance orifice

Ds inches Internal diameter of the stack at sampling location

DE percent Destruction efficiency

H inches H2O Average pressure differential across the meter orifice

H@ inches H2O Orifice pressure differential that corresponds to 0.75

cfm of air at 68 °F and 29.92 inches of Hg

p inches H2O Velocity head of stack gas

Eanalyte lb./hour Emission rate of analyte, time basis

I percent Isokinetic sampling ratio expressed as percentage

KI dimensionless K-factor, ratio of DH to DP, ideal

Kp ft[(lb/lb-mol)(in.

Hg)]1/2

Type S pitot tube constant,

s[(°R)(in. H2O)]1/2 = 85.49

Lp cfm Measured post-test leakage rate of the sampling train

Md lb./lb.-mole Molecular weight of gas at the DGM

Ms lb./lb.-mole Molecular weight of gas at the stack
NOMENCLATURE

Symbol Units Description

Mw lb./lb.-mole Molecular weight of water,

= 18.0

manalyte mg Mass of analyte in the sample

n dimensionless Number of data points

P MMBtu Fuel firing rate

Pbar inches Hg Barometric pressure at measurement site

Pinput tons/hour Process dry mass input rate

pg inches H2O Gauge (static) pressure of stack gas

Pm inches Hg Absolute pressure of meter gases

Ps inches Hg Absolute pressure of stack gases

Pstd inches Hg Standard absolute pressure

= 29.92

Qa cfm Volumetric flow rate of actual stack gas

Qsd dscfm Volumetric flow rate of dry stack gas, standardized

R (in. Hg)(ft3

) Ideal gas constant,

(lb-mole)(°R) = 21.85

RA percent Relative accuracy

RE percent Removal efficiency

RM ppm Average reference method concentration

rw lb/mL Density of water,

= 0.002201

ra g/mL Density of acetone,

= 0.7899

Sd dimensionless Standard deviation

Tm °R Absolute temperature of dry gas meter

Ts °R Absolute temperature of stack gas

Tstd °R Standard absolute temperature,

= 528

t0.975 dimensionless 2.5 percent error t-value

tm °F Temperature of DGM

ts °F Temperature of stack gas  minutes Total sampling time
NOMENCLATURE

Symbol Units Description

Vlc mL Total volume of liquid collected

Vm dcf Volume of gas sample as measured by the DGM

Vm(std) dscf Volume of gas sample as measured by the DGM,

standardized

Vw(std) scf Volume of water vapor in the gas sample,

standardized

vs ft./sec Velocity of stack gas

Ym dimensionless DGM calibration coefficient

Yc dimensionless DGM calibration check value

Yw dimensionless Reference (wet) gas meter calibration coefficient

% CO2 percent Percent CO2 by volume, dry basis

% O2 percent Percent O2 by volume, dry basis

% N2 percent Percent N2 by volume, dry basis
APPENDIX D

FIELD DATA
Client:

Location:

Source: 0.954

Test Team:

EPA Methods:

Ds (in.):

% O2

% CO2

Start Run:

End Run:

Run Number: 1 4.0 3.9

*K-factor change

Meter Last tm Filter Vacuum

(dcf) Impinger Average Exit (in. Hg)

Probe Assembly ID: P6-01

Dn (in.):

29.89

20.800

0.200

pg (in. H2O):

10.0

Temperature Readings (°F)

Filter

Inches H2O

Baghouse No. 5

B-01

0.250

Sampling Box ID:

Point H ( p)1/2

Test Date:

WLN, CS, RD

1, 2, 3A, 4, 26A

59.0

8:00 AM

p

Pbar (in. Hg):

ts

Minutes/Point:

K-Factor:

2.0

2:40 PM

Assumed Bws:

-1.10

Advanced Industrial Resources, Inc.

Method 5, 26A Field Data Sheet

1.973

Novelis

Greensboro, Georgia

February 22, 2012

Ym / H@:

Console ID: C-008

25 1055.84 1.70 6.80 1.304 170 253 56 85 248 4.0

26* 1070.92 1.20 4.68 1.095 166 255 57 86 249 3.0

27 1084.03 1.00 3.90 1.000 169 256 57 86 250 3.0

28 1095.31 0.88 3.43 0.938 173 264 57 85 251 2.0

29 1106.11 0.71 2.77 0.843 170 260 58 85 252 2.0

30 1116.00 1116.00 0.57 2.22 0.755 164 269 60 85 254 2.0

31 1124.69 0.39 1.52 0.624 155 259 60 85 249 1.0

32 1131.81 0.33 1.29 0.574 147 258 61 86 250 1.0

33 1138.30 0.35 1.37 0.592 142 258 61 85 252 1.0

34 1144.72 0.33 1.29 0.574 140 254 62 85 249 1.0

35 1151.18 0.36 1.40 0.600 140 257 62 86 251 1.0

36 1157.80 0.32 1.25 0.566 142 258 63 86 248 1.0

38 1164.72 1.30 5.07 1.140 143 256 64 85 250 4.0

39 1177.41 1.05 4.10 1.025 142 258 65 86 249 3.0

40 1189.22 0.81 3.16 0.900 124 253 61 85 248 2.0

End 1199.616

Theoretical maximum moisture collection at saturation (ml):

KR1710.3

Total moisture collected (mL):

Post System Leak Check (cfm):

90.0

0.006

Pre System Leak Check (cfm): 0.003
Client:

Location:

Source: 0.954

Test Team:

EPA Methods:

Ds (in.):

% O2

% CO2

Start Run:

End Run:

Run Number: 2

Meter Last tm Filter Vacuum

(dcf) Impinger Average Exit (in. Hg)

1 202.330 1.60 6.24 1.265 111 252 54 80 248 4.0

2 215.99 1.50 5.85 1.225 117 256 52 81 249 3.0

3 229.46 1.00 3.90 1.000 157 254 52 81 251 2.0

4 240.13 0.85 3.32 0.922 162 256 52 81 250 2.0

5 251.74 0.74 2.89 0.860 161 257 53 82 248 2.0

6 261.67 0.63 2.46 0.794 158 254 54 82 250 2.0

pg (in. H2O):

Point p H ( p)1/2 Filter

Dn (in.): 0.250

Temperature Readings (°F)

59.0

29.89

Assumed Bws: 2.0

Pbar (in. Hg):

3.9

Test Date: February 22, 2012

-1.10

Minutes/Point:

ts

10.0

Inches H2O

K-Factor:

20.800

3:10 PM

10:20 PM

0.200

Advanced Industrial Resources, Inc.

Method 5, 26A Field Data Sheet

Greensboro, Georgia Console ID: C-008

Novelis

P6-01

Ym / H@:

Probe Assembly ID:

WLN, CS, RD

1, 2, 3A, 4, 26A

1.973

Sampling Box ID: B-01

Baghouse No. 5

6 261.67 0.63 2.46 0.794 158 254 54 82 250 2.0

7 271.02 0.39 1.52 0.624 155 252 54 82 250 1.0

8 278.69 0.34 1.33 0.583 157 256 55 83 251 1.0

9 285.74 0.35 1.37 0.592 154 252 56 83 250 1.0

10 292.77 0.32 1.25 0.566 155 258 56 84 252 1.0

11 299.65 0.32 1.25 0.566 157 256 56 84 248 1.0

12 306.82 0.30 1.17 0.548 151 259 57 85 250 1.0

13 315.26 1.55 6.05 1.245 159 254 57 85 250 4.0

14 330.98 1.20 4.68 1.095 162 259 56 86 251 3.0

15 343.80 1.00 3.90 1.000 153 255 56 86 249 2.0

16 355.42 0.71 2.77 0.843 145 253 57 86 250 2.0

17 365.38 0.52 2.03 0.721 144 260 58 87 251 2.0

18 374.28 0.48 1.87 0.693 129 261 58 87 249 2.0

19 381.82 0.42 1.64 0.648 132 256 58 88 251 1.0

20 389.15 0.49 1.91 0.700 136 258 59 88 248 1.0

21 397.38 0.80 3.12 0.894 135 254 59 88 250 2.0

22 407.47 0.80 3.12 0.894 116 259 60 88 251 2.0

23 417.88 0.71 2.77 0.843 130 253 60 89 249 2.0

24 427.59 0.65 2.54 0.806 137 251 61 89 251 2.0
Client:

Location:

Source: 0.954

Test Team:

EPA Methods:

Ds (in.):

% O2

% CO2

Start Run:

End Run:

Run Number: 2

Meter Last tm Filter Vacuum

(dcf) Impinger Average Exit (in. Hg)

pg (in. H2O):

Point p H ( p)1/2 Filter

Dn (in.): 0.250

Temperature Readings (°F)

59.0

29.89

Assumed Bws: 2.0

Pbar (in. Hg):

3.9

Test Date: February 22, 2012

-1.10

Minutes/Point:

ts

10.0

Inches H2O

K-Factor:

20.800

3:10 PM

10:20 PM

0.200

Advanced Industrial Resources, Inc.

Method 5, 26A Field Data Sheet

Greensboro, Georgia Console ID: C-008

Novelis

P6-01

Ym / H@:

Probe Assembly ID:

WLN, CS, RD

1, 2, 3A, 4, 26A

1.973

Sampling Box ID: B-01

Baghouse No. 5

25 434.82 1.60 6.24 1.265 134 264 58 90 253 4.0

26 449.42 1.40 5.46 1.183 136 255 59 90 249 4.0

27 463.11 1.10 4.29 1.049 142 253 57 88 248 3.0

28 476.20 0.63 2.46 0.794 146 258 59 89 250 2.0

29 485.37 0.55 2.15 0.742 139 256 54 90 251 2.0

30 493.92 0.43 1.68 0.656 147 260 53 90 250 1.0

31 501.68 0.38 1.48 0.616 151 254 54 90 252 1.0

32 508.61 0.40 1.56 0.632 144 259 54 90 250 1.0

33 515.31 0.62 2.42 0.787 156 257 55 89 251 2.0

34 524.27 0.76 2.96 0.872 152 263 56 89 250 2.0

35 534.14 0.64 2.50 0.800 149 255 56 88 249 2.0

36 543.19 0.59 2.30 0.768 151 260 56 88 250 2.0

37 550.13 1.45 5.66 1.204 146 258 51 86 252 4.0

38 563.62 1.45 5.66 1.204 145 251 51 87 248 4.0

39 577.03 0.96 3.74 0.980 149 256 52 88 250 3.0

40 588.40 0.81 3.16 0.900 153 258 52 88 251 2.0

41 599.12 0.69 2.69 0.831 156 254 53 88 250 2.0

42 608.59 0.56 2.18 0.748 121 264 54 88 252 1.0

End 617.214

Theoretical maximum moisture collection at saturation (ml):

KR0.008

Pre System Leak Check (cfm): 0.006

2360.1

Post System Leak Check (cfm):

Total moisture collected (mL): 93.1
Client:

Location:

Source: 0.954

Test Team:

EPA Methods:

Ds (in.):

% O2

% CO2

Start Run:

End Run:

Run Number: 3

Meter Last tm Filter Vacuum

(dcf) Impinger Average Exit (in. Hg)

1 617.614 1.20 4.68 1.095 117 259 62 65 250 3.0

2 629.79 1.05 4.10 1.025 117 256 60 68 251 2.0

3 641.32 0.88 3.43 0.938 138 261 60 75 252 2.0

4 652.02 0.60 2.34 0.775 149 254 61 76 249 2.0

5 661.03 0.42 1.64 0.648 157 262 59 78 252 1.0

6 668.30 0.42 1.64 0.648 156 258 58 80 251 1.0

K-Factor:

ts

3.9

Filter

10.0

Temperature Readings (°F)

3:30 PM

( p)1/2 Point p H

Dn (in.):

Minutes/Point:

Inches H2O

59.0 0.250

9:20 AM pg (in. H2O): -1.10

0.000

20.900

Pbar (in. Hg): 29.84

Assumed Bws: 2.0

Advanced Industrial Resources, Inc.

Method 5, 26A Field Data Sheet

Novelis Test Date: February 23, 2012

1, 2, 3A, 4, 26A P6-01

B-01

Probe Assembly ID:

WLN, CS, RD Sampling Box ID:

Greensboro, Georgia Console ID: C-008

Baghouse No. 5 Ym / DH@: 1.973

6 668.30 0.42 1.64 0.648 156 258 58 80 251 1.0

7 675.88 0.75 2.93 0.866 153 258 60 81 252 2.0

8 685.74 1.00 3.90 1.000 156 256 60 83 249 2.0

9 697.34 1.00 3.90 1.000 160 264 61 86 253 2.0

10 709.02 1.10 4.29 1.049 160 261 62 89 252 2.0

11 721.06 0.68 2.65 0.825 161 258 63 90 250 2.0

12 730.55 0.59 2.30 0.768 160 257 63 91 251 2.0

13 739.56 1.80 7.02 1.342 166 256 61 92 250 5.0

14 754.73 1.45 5.66 1.204 164 262 58 94 252 4.0

15 768.61 1.10 4.29 1.049 165 257 54 95 249 3.0

16 780.68 0.90 3.51 0.949 166 257 54 99 254 3.0

17 791.92 0.93 3.63 0.964 167 261 55 99 252 3.0

18 803.32 0.48 1.87 0.693 170 258 54 101 251 2.0

19 811.20 0.30 1.17 0.548 169 257 57 100 250 1.0

20 817.73 0.30 1.17 0.548 167 259 58 99 252 1.0

21 823.72 0.34 1.33 0.583 173 264 58 97 259 1.0

22 830.41 0.37 1.44 0.608 153 254 60 96 251 1.0

23 837.64 0.33 1.29 0.574 152 262 61 96 252 1.0

24 843.92 0.33 1.29 0.574 152 257 61 95 253 1.0
Client:

Location:

Source: 0.954

Test Team:

EPA Methods:

Ds (in.):

% O2

% CO2

Start Run:

End Run:

Run Number: 3

Meter Last tm Filter Vacuum

(dcf) Impinger Average Exit (in. Hg)

K-Factor:

ts

3.9

Filter

10.0

Temperature Readings (°F)

3:30 PM

( p)1/2 Point p H

Dn (in.):

Minutes/Point:

Inches H2O

59.0 0.250

9:20 AM pg (in. H2O): -1.10

0.000

20.900

Pbar (in. Hg): 29.84

Assumed Bws: 2.0

Advanced Industrial Resources, Inc.

Method 5, 26A Field Data Sheet

Novelis Test Date: February 23, 2012

1, 2, 3A, 4, 26A P6-01

B-01

Probe Assembly ID:

WLN, CS, RD Sampling Box ID:

Greensboro, Georgia Console ID: C-008

Baghouse No. 5 Ym / DH@: 1.973

25 850.59 1.50 5.85 1.225 169 260 59 94 253 4.0

26 864.09 1.60 6.24 1.265 180 250 61 95 252 5.0

27 878.30 1.20 4.68 1.095 175 259 62 96 253 3.0

28 891.15 1.05 4.10 1.025 172 254 57 97 254 3.0

29 903.07 0.84 3.28 0.917 170 264 57 97 252 2.0

30 914.03 0.51 1.99 0.714 173 257 58 98 252 2.0

31 922.61 0.33 1.29 0.574 175 259 60 98 254 1.0

32 929.38 0.35 1.37 0.592 170 267 61 98 251 1.0

33 936.08 0.37 1.44 0.608 162 259 61 98 250 1.0

34 943.27 0.35 1.37 0.592 160 257 61 99 251 1.0

35 950.31 0.35 1.37 0.592 158 263 61 99 253 1.0

36 957.32 0.27 1.05 0.520 141 263 62 100 253 1.0

End 963.547

Theoretical maximum moisture collection at saturation (ml):

Post System Leak Check (cfm): 0.002

Pre System Leak Check (cfm): 0.002

3198.0

Total moisture collected (mL): 141.7
Client: Date:

Location: Ds

 (in.):

Source: As

 (ft2):

Test Team: Dn

 (in.):

Probe ID: An

 (ft2):

Cp:

tm (°F): p

Console ID: (in. H2O) (degrees)

Ym: 1 0.0 0.0

H@: 2 0.0 0.0

Assumed Bws: 3 0.0 0.0

Pbar (in. Hg): 4 0.0 2.0

5 0.0 4.0

6 0.0 0.0

7 0.0 5.0

8 0.0 2.0

9 0.0 0.0

Greensboro, Georgia 59.0

Advanced Industrial Resources, Inc.

Cyclonic Flow Absence Verification Field Data

EPA Method 1

Novelis February 22, 2012

Baghouse No. 5 18.99

0.84

C-008

70

P6-01 0.000341

1.973

9.540

2%

Point

WLN, CS, RD 0.250

29.89

9 0.0 0.0

10 0.0 0.0

11 0.0 2.0

12 0.0 0.0

1 0.0 0.0

2 0.0 0.0

3 0.0 2.0

4 0.0 0.0

5 0.0 6.0

6 0.0 5.0

7 0.0 0.0

8 0.0 2.0

9 0.0 0.0

10 0.0 4.0

11 0.0 0.0

12 0.0 2.0

Change Ports
Client: Date:

Location: Test Team:

Source:

Dn (in.): p t

s An

 (ft2): (in. H2O) (°F)

Ds (in.): 1 1.40 113

As (ft2): 2 1.10 108

Length A (in.): 3 0.85 110

Length B (in.): 4 0.66 114

tamb (°F): 5 0.52 111

Assumed Bws: 6 0.50 116

Pbar (in. Hg): 7 0.37 120

Pg (in. H2O): 8 0.46 118

% O2: 9 0.54 119

% CO2: 10 0.82 121

Console ID: 11 0.74 126

Y: 12 0.69 128

H@:

9.540

0.84

1.973

Point

Advanced Industrial Resources, Inc.

Source Description Sheets

Baghouse No. 5

Novelis February 22, 2012

Greensboro, Georgia WLN, CS, RD

59.0

0.250

29.89

C-008

20.00%

84

0.000341

18.99

180

2%

20.8%

Change Ports

60

-1.10

H@:

Cp: 1 2.00 126

K-Factor: 2 1.55 120

3 1.00 129

4 0.88 134

5 0.71 137

6 0.60 143

7 0.33 142

8 0.35 141

9 0.35 150

10 0.32 154

11 0.30 154

12 0.32 160 < A= > < B= >

Sampling Location

0.84

1.973

4.0

Change Ports

Sketch of Stack

Digital Photograph of Source Not Available
59.0 Inch Diameter Stack

Traverse Point Locations

Baghouse No. 5

Novelis

for

59.0 Inch Diameter Stack

Two Ports at 900

Sampling Point

1 1.2

2 4.0

3 7.0

4 10.4

5 14.8

6 21.0

7 38.0

8 44.3

9 48.6

10 52.0

11 55.0

12 57.8

Distance from

Stack Wall (inches)








APPENDIX E

LABORATORY REPORTS

























































APPENDIX F

CALIBRATION DATA





















APPENDIX G

PROCESS OPERATION DATA
Test Ave.

Start time 2/22/2012 8:00 2/22/2012 15:10 2/23/2012 9:20

End Time 2/22/2012 14:40 2/22/2012 22:20 2/23/2012 15:30

Cast ID 120222C 120222E 120223C

FCE 3 Inputs Test 1 Test 2 Test 3

RSI/Prime (lbs) 9534 8172 0 5,902

Uncoated Manual Charge Scrap (lbs) 37138 43080 47602 42,607

Decoated UBC (lbs) 0 0 0 0

Coated Scrap (lbs) 32,243 43,758 20,732 32,244

Total Aluminum Input 78,915 95,010 68,334 80,753

Salt: A103-2 (51.58% Chloride) 2102 2354 2487

Salt: Amlox 371 (55.52% Chloride) 0 0 0

Total Salt Input 2102 2354 2487 2314

Total Available Chloride 1084 1214 1283 1194

Test 1 Test 2 Test 3 Test Ave.

Total Production Output

FCE 1 inches transferred 12.9 0.0 8.5

FCE 2 inches transferred 6.9 13.4 12.8

FCE 3 inches transferred 10.8 12.9 11.2

Cast Weight (lbs) 247600 214400 214700

FCE 3 Total Output Production (lbs) 87388 105162 73989 88846

Test 1 Test 2 Test 3 Test Ave.

Baghouse

Ave. Inlet Temperature ('F) 154 143 192 163

Lime Feed Rate (Hz) 12 12 12 12

February 22 - 23, 2012
Volume

Transferred

Time Event

Melter units "

Holder Units lbs Cast ID Product

Melter Weight

Production lbs

2/22/2012 0400 FCE1 xfer to holder 8.6

2/22/2012 0400 FCE2 xfer to holder 13.4

2/22/2012 0408 FCE3 xfer to holder 8

2/22/2012 0640 Holder Cast 215100 120222A 3104

2/22/2012 0745 FCE3 xfer to holder 6.5 44595

2/22/2012 0800 start 1st sample run

2/22/2012 0953 FCE2 xfer to holder 13.7 93994

2/22/2012 1000 FCE1 xfer to holder 10.7 73411

2/22/2012 1304 Holder Cast 212000 120222B 3104

2/22/2012 1435 FCE3 xfer to holder 10.8 87388

2/22/2012 1440 end 1st sample run 87,388 FCE3 production 1st run, lbs

2/22/2012 1457 FCE2 xfer to holder 2 16183

2/22/2012 1510 start 2nd sample run

2/22/2012 1607 FCE1 xfer to holder 12.9 104380

2/22/2012 1623 FCE2 xfer to holder 4.9 39648

2/22/2012 1741 Holder Cast 32400 120222C 3104

2/22/2012 2158 Holder Cast 215200 120222D 3104

2/22/2012 2205 FCE3 xfer to holder 12.9 105162

2/22/2012 2220 end 2nd sample run 105,162 FCE3 production 2nd run, lbs

2/22/2012 2225 FCE2 xfer to holder 12.5 101901

2/22/2012 2321 FCE2 xfer to holder 0.9 7337

2/23/2012 0139 Holder Cast 214400 120222E 3104

2/23/2012 0424 FCE2 xfer to holder 13

2/23/2012 0425 FCE1 xfer to holder 11

2/23/2012 0430 FCE3 xfer to holder 4.1

2/23/2012 0648 Holder Cast 213700 120223A 3104

2/23/2012 0845 FCE3 xfer to holder 4.3

2/23/2012 0920 start 3rd sample run

2/23/2012 1056 FCE2 xfer to holder 13

2/23/2012 1100 FCE1 xfer to holder 11.2

2/23/2012 1319 Holder Cast 211600 120223B 3104

2/23/2012 1525 FCE1 xfer to holder 8.5 56152

2/23/2012 1525 FCE3 xfer to holder 11.2 73989

2/23/2012 1530 FCE2 xfer to holder 12.8 84559

2/23/2012 1530 end 3rd sample run 73,989 FCE3 production 3rd run, lbs
2/23/2012 1750 Holder Cast 214700 120223C 3104
Baghouse 5 Emissions Tests

February 22 - 23, 2011

Test Run Run 1 Run 2 Run 3

Start Time

End Time

Inputs (lbs)

RSI/Prime 9534 8172 0

Uncoated Scrap 37138 43080 47602

Decoated UBC 0 0 0

Coated Scrap 32243 43758 20732

Total Aluminum Input 78915 95010 68334

Salt

A103-2 2102 2354 2487

Amlox 371 0 0 0

FCE3 inches transferred 10.8 12.9 11.2

Total coated: 32243

Furnace #3 sidewell scrap lbs Total uncoated: 37138

Class1 1070 Class2

37138 0 10748 21495

28258 10748 21495

8880

Total coated: 43758

2/22/12 10:20 PM 2/23/12 3:30 PM

Run 1 Metal Input Batches

Run 2 Metal Input Batches

2/22/12 8:00 AM 2/22/12 3:10 PM 2/23/12 9:20 AM

2/22/12 2:40 PM

Total coated: 43758

Furnace #3 sidewell scrap lbs Total uncoated: 43080

Class1 Class2 1070

43080 43758 1200

17040 32658 1200

5220 11100

5100

5170

5300

5250

Total coated: 20732

Furnace #3 sidewell scrap lbs Total uncoated: 47602

Class1 EC Wire 1070 Class2

42160 5442 0 20732

42160 2712 5250

2383 5120

347 5216

5146

Run 3 Metal Input Batches

Run 2 Metal Input Batches
Bag House #5 Inlet Temperatures (°F) Test 1 Test 2 Test 3 Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average

153.75 2/22/12 8:00 AM 112 153.65 143.27 2/22/12 3:10 PM 115 143.21 192.39 2/23/12 9:20 AM 124 192.25

2/22/12 8:01 AM 112 2/22/12 3:11 PM 114 2/23/12 9:21 AM 125

2/22/12 8:02 AM 111 2/22/12 3:12 PM 114 2/23/12 9:22 AM 126

2/22/12 8:03 AM 109 2/22/12 3:13 PM 115 2/23/12 9:23 AM 126

2/22/12 8:04 AM 108 2/22/12 3:14 PM 116 2/23/12 9:24 AM 127

2/22/12 8:05 AM 106 2/22/12 3:15 PM 117 2/23/12 9:25 AM 128

2/22/12 8:06 AM 105 2/22/12 3:16 PM 119 2/23/12 9:26 AM 128

2/22/12 8:07 AM 105 2/22/12 3:17 PM 121 2/23/12 9:27 AM 129

2/22/12 8:08 AM 104 2/22/12 3:18 PM 122 2/23/12 9:28 AM 129

2/22/12 8:09 AM 103 2/22/12 3:19 PM 123 2/23/12 9:29 AM 129

2/22/12 8:10 AM 101 2/22/12 3:20 PM 124 2/23/12 9:30 AM 130

2/22/12 8:11 AM 101 2/22/12 3:21 PM 124 2/23/12 9:31 AM 130

2/22/12 8:12 AM 100 2/22/12 3:22 PM 124 2/23/12 9:32 AM 129

2/22/12 8:13 AM 99 2/22/12 3:23 PM 124 2/23/12 9:33 AM 128

2/22/12 8:14 AM 98 2/22/12 3:24 PM 125 2/23/12 9:34 AM 129

2/22/12 8:15 AM 98 2/22/12 3:25 PM 127 2/23/12 9:35 AM 129

2/22/12 8:16 AM 97 2/22/12 3:26 PM 129 2/23/12 9:36 AM 130

2/22/12 8:17 AM 97 2/22/12 3:27 PM 132 2/23/12 9:37 AM 130

2/22/12 8:18 AM 99 2/22/12 3:28 PM 135 2/23/12 9:38 AM 130

2/22/12 8:19 AM 100 2/22/12 3:29 PM 139 2/23/12 9:39 AM 131

2/22/12 8:20 AM 102 2/22/12 3:30 PM 142 2/23/12 9:40 AM 132

2/22/12 8:21 AM 103 2/22/12 3:31 PM 145 2/23/12 9:41 AM 134

2/22/12 8:22 AM 104 2/22/12 3:32 PM 148 2/23/12 9:42 AM 137

2/22/12 8:23 AM 105 2/22/12 3:33 PM 151 2/23/12 9:43 AM 139

2/22/12 8:24 AM 105 2/22/12 3:34 PM 154 2/23/12 9:44 AM 141

2/22/12 8:25 AM 105 2/22/12 3:35 PM 156 2/23/12 9:45 AM 143

2/22/12 8:26 AM 104 2/22/12 3:36 PM 158 2/23/12 9:46 AM 145

2/22/12 8:27 AM 104 2/22/12 3:37 PM 160 2/23/12 9:47 AM 147

2/22/12 8:28 AM 103 2/22/12 3:38 PM 162 2/23/12 9:48 AM 149

2/22/12 8:29 AM 102 2/22/12 3:39 PM 164 2/23/12 9:49 AM 150

2/22/12 8:30 AM 102 2/22/12 3:40 PM 165 2/23/12 9:50 AM 151

2/22/12 8:31 AM 101 2/22/12 3:41 PM 166 2/23/12 9:51 AM 153

2/22/12 8:32 AM 100 2/22/12 3:42 PM 167 2/23/12 9:52 AM 155

2/22/12 8:33 AM 100 2/22/12 3:43 PM 168 2/23/12 9:53 AM 156

2/22/12 8:34 AM 99 2/22/12 3:44 PM 169 2/23/12 9:54 AM 158

2/22/12 8:35 AM 98 2/22/12 3:45 PM 170 2/23/12 9:55 AM 159

2/22/12 8:36 AM 98 2/22/12 3:46 PM 170 2/23/12 9:56 AM 160

2/22/12 8:37 AM 97 2/22/12 3:47 PM 171 2/23/12 9:57 AM 161

2/22/12 8:38 AM 96 2/22/12 3:48 PM 172 2/23/12 9:58 AM 162

2/22/12 8:39 AM 96 2/22/12 3:49 PM 172 2/23/12 9:59 AM 163

2/22/12 8:40 AM 96 2/22/12 3:50 PM 173 2/23/12 10:00 AM 164

2/22/12 8:41 AM 2/22/12 8:41 AM 95 2/22/12 3:51 PM 2/22/12 3:51 PM 173 2/23/12 10:01 AM 2/23/12 10:01 AM 165

2/22/12 8:42 AM 94 2/22/12 3:52 PM 174 2/23/12 10:02 AM 166

2/22/12 8:43 AM 95 2/22/12 3:53 PM 174 2/23/12 10:03 AM 167

2/22/12 8:44 AM 96 2/22/12 3:54 PM 175 2/23/12 10:04 AM 168

2/22/12 8:45 AM 97 2/22/12 3:55 PM 175 2/23/12 10:05 AM 169

2/22/12 8:46 AM 99 2/22/12 3:56 PM 175 2/23/12 10:06 AM 170

2/22/12 8:47 AM 101 2/22/12 3:57 PM 176 2/23/12 10:07 AM 170

2/22/12 8:48 AM 103 2/22/12 3:58 PM 176 2/23/12 10:08 AM 171

2/22/12 8:49 AM 104 2/22/12 3:59 PM 176 2/23/12 10:09 AM 171

2/22/12 8:50 AM 104 2/22/12 4:00 PM 177 2/23/12 10:10 AM 172

2/22/12 8:51 AM 104 2/22/12 4:01 PM 177 2/23/12 10:11 AM 173

2/22/12 8:52 AM 103 2/22/12 4:02 PM 177 2/23/12 10:12 AM 173

2/22/12 8:53 AM 103 2/22/12 4:03 PM 177 2/23/12 10:13 AM 174

2/22/12 8:54 AM 102 2/22/12 4:04 PM 177 2/23/12 10:14 AM 175

2/22/12 8:55 AM 101 2/22/12 4:05 PM 178 2/23/12 10:15 AM 175

2/22/12 8:56 AM 101 2/22/12 4:06 PM 178 2/23/12 10:16 AM 174

2/22/12 8:57 AM 100 2/22/12 4:07 PM 178 2/23/12 10:17 AM 173

2/22/12 8:58 AM 100 2/22/12 4:08 PM 178 2/23/12 10:18 AM 172

2/22/12 8:59 AM 99 2/22/12 4:09 PM 178 2/23/12 10:19 AM 172

2/22/12 9:00 AM 98 2/22/12 4:10 PM 178 2/23/12 10:20 AM 171

2/22/12 9:01 AM 97 2/22/12 4:11 PM 178 2/23/12 10:21 AM 171

2/22/12 9:02 AM 96 2/22/12 4:12 PM 178 2/23/12 10:22 AM 171

2/22/12 9:03 AM 96 2/22/12 4:13 PM 178 2/23/12 10:23 AM 171

2/22/12 9:04 AM 96 2/22/12 4:14 PM 177 2/23/12 10:24 AM 172

2/22/12 9:05 AM 96 2/22/12 4:15 PM 177 2/23/12 10:25 AM 173

2/22/12 9:06 AM 97 2/22/12 4:16 PM 177 2/23/12 10:26 AM 174

2/22/12 9:07 AM 99 2/22/12 4:17 PM 176 2/23/12 10:27 AM 175

2/22/12 9:08 AM 100 2/22/12 4:18 PM 176 2/23/12 10:28 AM 175

2/22/12 9:09 AM 100 2/22/12 4:19 PM 175 2/23/12 10:29 AM 176

2/22/12 9:10 AM 101 2/22/12 4:20 PM 175 2/23/12 10:30 AM 177

2/22/12 9:11 AM 101 2/22/12 4:21 PM 175 2/23/12 10:31 AM 178

2/22/12 9:12 AM 102 2/22/12 4:22 PM 174 2/23/12 10:32 AM 179

2/22/12 9:13 AM 102 2/22/12 4:23 PM 174 2/23/12 10:33 AM 180

2/22/12 9:14 AM 102 2/22/12 4:24 PM 175 2/23/12 10:34 AM 181

2/22/12 9:15 AM 101 2/22/12 4:25 PM 175 2/23/12 10:35 AM 182

2/22/12 9:16 AM 100 2/22/12 4:26 PM 175 2/23/12 10:36 AM 183

2/22/12 9:17 AM 100 2/22/12 4:27 PM 177 2/23/12 10:37 AM 185

2/22/12 9:18 AM 100 2/22/12 4:28 PM 179 2/23/12 10:38 AM 186

2/22/12 9:19 AM 100 2/22/12 4:29 PM 180 2/23/12 10:39 AM 186

2/22/12 9:20 AM 101 2/22/12 4:30 PM 180 2/23/12 10:40 AM 187

2/22/12 9:21 AM 101 2/22/12 4:31 PM 180 2/23/12 10:41 AM 188

2/22/12 9:22 AM 102 2/22/12 4:32 PM 179 2/23/12 10:42 AM 189

2/22/12 9:23 AM 103 2/22/12 4:33 PM 179 2/23/12 10:43 AM 189

2/22/12 9:24 AM 105 2/22/12 4:34 PM 179 2/23/12 10:44 AM 190
Bag House #5 Inlet Temperatures (°F) Test 1 Test 2 Test 3 Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average

2/22/12 9:25 AM 108 2/22/12 4:35 PM 179 2/23/12 10:45 AM 191

2/22/12 9:26 AM 110 2/22/12 4:36 PM 179 2/23/12 10:46 AM 191

2/22/12 9:27 AM 112 2/22/12 4:37 PM 179 2/23/12 10:47 AM 191

2/22/12 9:28 AM 114 2/22/12 4:38 PM 179 2/23/12 10:48 AM 191

2/22/12 9:29 AM 116 2/22/12 4:39 PM 179 2/23/12 10:49 AM 192

2/22/12 9:30 AM 117 2/22/12 4:40 PM 180 2/23/12 10:50 AM 192

2/22/12 9:31 AM 119 2/22/12 4:41 PM 180 2/23/12 10:51 AM 193

2/22/12 9:32 AM 121 2/22/12 4:42 PM 179 2/23/12 10:52 AM 194

2/22/12 9:33 AM 123 2/22/12 4:43 PM 179 2/23/12 10:53 AM 194

2/22/12 9:34 AM 125 2/22/12 4:44 PM 178 2/23/12 10:54 AM 195

2/22/12 9:35 AM 126 2/22/12 4:45 PM 178 2/23/12 10:55 AM 195

2/22/12 9:36 AM 128 2/22/12 4:46 PM 178 2/23/12 10:56 AM 196

2/22/12 9:37 AM 130 2/22/12 4:47 PM 177 2/23/12 10:57 AM 196

2/22/12 9:38 AM 131 2/22/12 4:48 PM 177 2/23/12 10:58 AM 196

2/22/12 9:39 AM 133 2/22/12 4:49 PM 177 2/23/12 10:59 AM 197

2/22/12 9:40 AM 134 2/22/12 4:50 PM 177 2/23/12 11:00 AM 197

2/22/12 9:41 AM 134 2/22/12 4:51 PM 176 2/23/12 11:01 AM 198

2/22/12 9:42 AM 135 2/22/12 4:52 PM 175 2/23/12 11:02 AM 199

2/22/12 9:43 AM 136 2/22/12 4:53 PM 174 2/23/12 11:03 AM 199

2/22/12 9:44 AM 136 2/22/12 4:54 PM 171 2/23/12 11:04 AM 200

2/22/12 9:45 AM 136 2/22/12 4:55 PM 169 2/23/12 11:05 AM 200

2/22/12 9:46 AM 137 2/22/12 4:56 PM 166 2/23/12 11:06 AM 202

2/22/12 9:47 AM 137 2/22/12 4:57 PM 164 2/23/12 11:07 AM 202

2/22/12 9:48 AM 138 2/22/12 4:58 PM 161 2/23/12 11:08 AM 202

2/22/12 9:49 AM 138 2/22/12 4:59 PM 158 2/23/12 11:09 AM 202

2/22/12 9:50 AM 138 2/22/12 5:00 PM 157 2/23/12 11:10 AM 201

2/22/12 9:51 AM 139 2/22/12 5:01 PM 156 2/23/12 11:11 AM 199

2/22/12 9:52 AM 138 2/22/12 5:02 PM 155 2/23/12 11:12 AM 197

2/22/12 9:53 AM 136 2/22/12 5:03 PM 155 2/23/12 11:13 AM 195

2/22/12 9:54 AM 134 2/22/12 5:04 PM 155 2/23/12 11:14 AM 193

2/22/12 9:55 AM 132 2/22/12 5:05 PM 156 2/23/12 11:15 AM 192

2/22/12 9:56 AM 129 2/22/12 5:06 PM 156 2/23/12 11:16 AM 192

2/22/12 9:57 AM 127 2/22/12 5:07 PM 157 2/23/12 11:17 AM 193

2/22/12 9:58 AM 125 2/22/12 5:08 PM 157 2/23/12 11:18 AM 193

2/22/12 9:59 AM 123 2/22/12 5:09 PM 158 2/23/12 11:19 AM 194

2/22/12 10:00 AM 123 2/22/12 5:10 PM 158 2/23/12 11:20 AM 195

2/22/12 10:01 AM 124 2/22/12 5:11 PM 158 2/23/12 11:21 AM 195

2/22/12 10:02 AM 125 2/22/12 5:12 PM 158 2/23/12 11:22 AM 196

2/22/12 10:03 AM 125 2/22/12 5:13 PM 159 2/23/12 11:23 AM 197

2/22/12 10:04 AM 126 2/22/12 5:14 PM 159 2/23/12 11:24 AM 198

2/22/12 10:05 AM 127 2/22/12 5:15 PM 159 2/23/12 11:25 AM 199

2/22/12 10:06 AM 2/22/12 10:06 AM 128 2/22/12 5:16 PM 2/22/12 5:16 PM 159 2/23/12 11:26 AM 2/23/12 11:26 AM 199

2/22/12 10:07 AM 128 2/22/12 5:17 PM 160 2/23/12 11:27 AM 200

2/22/12 10:08 AM 129 2/22/12 5:18 PM 160 2/23/12 11:28 AM 201

2/22/12 10:09 AM 130 2/22/12 5:19 PM 161 2/23/12 11:29 AM 201

2/22/12 10:10 AM 130 2/22/12 5:20 PM 161 2/23/12 11:30 AM 202

2/22/12 10:11 AM 130 2/22/12 5:21 PM 162 2/23/12 11:31 AM 203

2/22/12 10:12 AM 129 2/22/12 5:22 PM 162 2/23/12 11:32 AM 203

2/22/12 10:13 AM 127 2/22/12 5:23 PM 163 2/23/12 11:33 AM 204

2/22/12 10:14 AM 126 2/22/12 5:24 PM 163 2/23/12 11:34 AM 205

2/22/12 10:15 AM 124 2/22/12 5:25 PM 164 2/23/12 11:35 AM 205

2/22/12 10:16 AM 122 2/22/12 5:26 PM 165 2/23/12 11:36 AM 205

2/22/12 10:17 AM 120 2/22/12 5:27 PM 166 2/23/12 11:37 AM 205

2/22/12 10:18 AM 119 2/22/12 5:28 PM 165 2/23/12 11:38 AM 206

2/22/12 10:19 AM 119 2/22/12 5:29 PM 164 2/23/12 11:39 AM 206

2/22/12 10:20 AM 118 2/22/12 5:30 PM 162 2/23/12 11:40 AM 206

2/22/12 10:21 AM 119 2/22/12 5:31 PM 160 2/23/12 11:41 AM 207

2/22/12 10:22 AM 120 2/22/12 5:32 PM 159 2/23/12 11:42 AM 207

2/22/12 10:23 AM 122 2/22/12 5:33 PM 156 2/23/12 11:43 AM 208

2/22/12 10:24 AM 123 2/22/12 5:34 PM 154 2/23/12 11:44 AM 208

2/22/12 10:25 AM 125 2/22/12 5:35 PM 152 2/23/12 11:45 AM 209

2/22/12 10:26 AM 126 2/22/12 5:36 PM 150 2/23/12 11:46 AM 208

2/22/12 10:27 AM 128 2/22/12 5:37 PM 148 2/23/12 11:47 AM 207

2/22/12 10:28 AM 129 2/22/12 5:38 PM 146 2/23/12 11:48 AM 205

2/22/12 10:29 AM 131 2/22/12 5:39 PM 144 2/23/12 11:49 AM 205

2/22/12 10:30 AM 132 2/22/12 5:40 PM 143 2/23/12 11:50 AM 204

2/22/12 10:31 AM 133 2/22/12 5:41 PM 143 2/23/12 11:51 AM 204

2/22/12 10:32 AM 134 2/22/12 5:42 PM 144 2/23/12 11:52 AM 204

2/22/12 10:33 AM 135 2/22/12 5:43 PM 145 2/23/12 11:53 AM 204

2/22/12 10:34 AM 134 2/22/12 5:44 PM 146 2/23/12 11:54 AM 205

2/22/12 10:35 AM 133 2/22/12 5:45 PM 147 2/23/12 11:55 AM 205

2/22/12 10:36 AM 132 2/22/12 5:46 PM 149 2/23/12 11:56 AM 205

2/22/12 10:37 AM 131 2/22/12 5:47 PM 150 2/23/12 11:57 AM 206

2/22/12 10:38 AM 131 2/22/12 5:48 PM 151 2/23/12 11:58 AM 206

2/22/12 10:39 AM 132 2/22/12 5:49 PM 152 2/23/12 11:59 AM 206

2/22/12 10:40 AM 132 2/22/12 5:50 PM 153 2/23/12 12:00 PM 207

2/22/12 10:41 AM 134 2/22/12 5:51 PM 154 2/23/12 12:01 PM 207

2/22/12 10:42 AM 136 2/22/12 5:52 PM 155 2/23/12 12:02 PM 208

2/22/12 10:43 AM 137 2/22/12 5:53 PM 156 2/23/12 12:03 PM 208

2/22/12 10:44 AM 138 2/22/12 5:54 PM 157 2/23/12 12:04 PM 209

2/22/12 10:45 AM 140 2/22/12 5:55 PM 157 2/23/12 12:05 PM 209

2/22/12 10:46 AM 141 2/22/12 5:56 PM 158 2/23/12 12:06 PM 210

2/22/12 10:47 AM 143 2/22/12 5:57 PM 159 2/23/12 12:07 PM 210

2/22/12 10:48 AM 144 2/22/12 5:58 PM 159 2/23/12 12:08 PM 211

2/22/12 10:49 AM 145 2/22/12 5:59 PM 159 2/23/12 12:09 PM 211
Bag House #5 Inlet Temperatures (°F) Test 1 Test 2 Test 3 Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average

2/22/12 10:50 AM 147 2/22/12 6:00 PM 159 2/23/12 12:10 PM 212

2/22/12 10:51 AM 148 2/22/12 6:01 PM 157 2/23/12 12:11 PM 212

2/22/12 10:52 AM 149 2/22/12 6:02 PM 155 2/23/12 12:12 PM 213

2/22/12 10:53 AM 150 2/22/12 6:03 PM 153 2/23/12 12:13 PM 213

2/22/12 10:54 AM 152 2/22/12 6:04 PM 151 2/23/12 12:14 PM 214

2/22/12 10:55 AM 153 2/22/12 6:05 PM 148 2/23/12 12:15 PM 214

2/22/12 10:56 AM 155 2/22/12 6:06 PM 146 2/23/12 12:16 PM 214

2/22/12 10:57 AM 156 2/22/12 6:07 PM 144 2/23/12 12:17 PM 214

2/22/12 10:58 AM 157 2/22/12 6:08 PM 141 2/23/12 12:18 PM 213

2/22/12 10:59 AM 158 2/22/12 6:09 PM 140 2/23/12 12:19 PM 212

2/22/12 11:00 AM 160 2/22/12 6:10 PM 140 2/23/12 12:20 PM 210

2/22/12 11:01 AM 160 2/22/12 6:11 PM 140 2/23/12 12:21 PM 210

2/22/12 11:02 AM 161 2/22/12 6:12 PM 140 2/23/12 12:22 PM 210

2/22/12 11:03 AM 162 2/22/12 6:13 PM 141 2/23/12 12:23 PM 209

2/22/12 11:04 AM 163 2/22/12 6:14 PM 142 2/23/12 12:24 PM 209

2/22/12 11:05 AM 164 2/22/12 6:15 PM 143 2/23/12 12:25 PM 209

2/22/12 11:06 AM 165 2/22/12 6:16 PM 144 2/23/12 12:26 PM 209

2/22/12 11:07 AM 166 2/22/12 6:17 PM 145 2/23/12 12:27 PM 210

2/22/12 11:08 AM 166 2/22/12 6:18 PM 146 2/23/12 12:28 PM 210

2/22/12 11:09 AM 167 2/22/12 6:19 PM 147 2/23/12 12:29 PM 211

2/22/12 11:10 AM 168 2/22/12 6:20 PM 148 2/23/12 12:30 PM 212

2/22/12 11:11 AM 169 2/22/12 6:21 PM 149 2/23/12 12:31 PM 212

2/22/12 11:12 AM 169 2/22/12 6:22 PM 149 2/23/12 12:32 PM 213

2/22/12 11:13 AM 169 2/22/12 6:23 PM 150 2/23/12 12:33 PM 213

2/22/12 11:14 AM 170 2/22/12 6:24 PM 150 2/23/12 12:34 PM 213

2/22/12 11:15 AM 170 2/22/12 6:25 PM 151 2/23/12 12:35 PM 214

2/22/12 11:16 AM 170 2/22/12 6:26 PM 152 2/23/12 12:36 PM 214

2/22/12 11:17 AM 171 2/22/12 6:27 PM 152 2/23/12 12:37 PM 214

2/22/12 11:18 AM 171 2/22/12 6:28 PM 153 2/23/12 12:38 PM 214

2/22/12 11:19 AM 173 2/22/12 6:29 PM 153 2/23/12 12:39 PM 214

2/22/12 11:20 AM 174 2/22/12 6:30 PM 154 2/23/12 12:40 PM 214

2/22/12 11:21 AM 174 2/22/12 6:31 PM 154 2/23/12 12:41 PM 215

2/22/12 11:22 AM 174 2/22/12 6:32 PM 155 2/23/12 12:42 PM 215

2/22/12 11:23 AM 174 2/22/12 6:33 PM 155 2/23/12 12:43 PM 215

2/22/12 11:24 AM 175 2/22/12 6:34 PM 156 2/23/12 12:44 PM 214

2/22/12 11:25 AM 175 2/22/12 6:35 PM 156 2/23/12 12:45 PM 214

2/22/12 11:26 AM 176 2/22/12 6:36 PM 156 2/23/12 12:46 PM 214

2/22/12 11:27 AM 177 2/22/12 6:37 PM 156 2/23/12 12:47 PM 213

2/22/12 11:28 AM 178 2/22/12 6:38 PM 156 2/23/12 12:48 PM 210

2/22/12 11:29 AM 179 2/22/12 6:39 PM 155 2/23/12 12:49 PM 208

2/22/12 11:30 AM 181 2/22/12 6:40 PM 153 2/23/12 12:50 PM 205

2/22/12 11:31 AM 2/22/12 11:31 AM 183 2/22/12 6:41 PM 2/22/12 6:41 PM 151 2/23/12 12:51 PM 2/23/12 12:51 PM 203

2/22/12 11:32 AM 184 2/22/12 6:42 PM 149 2/23/12 12:52 PM 200

2/22/12 11:33 AM 185 2/22/12 6:43 PM 146 2/23/12 12:53 PM 198

2/22/12 11:34 AM 186 2/22/12 6:44 PM 144 2/23/12 12:54 PM 195

2/22/12 11:35 AM 186 2/22/12 6:45 PM 141 2/23/12 12:55 PM 194

2/22/12 11:36 AM 187 2/22/12 6:46 PM 139 2/23/12 12:56 PM 192

2/22/12 11:37 AM 187 2/22/12 6:47 PM 137 2/23/12 12:57 PM 191

2/22/12 11:38 AM 188 2/22/12 6:48 PM 135 2/23/12 12:58 PM 189

2/22/12 11:39 AM 189 2/22/12 6:49 PM 133 2/23/12 12:59 PM 188

2/22/12 11:40 AM 190 2/22/12 6:50 PM 131 2/23/12 1:00 PM 188

2/22/12 11:41 AM 190 2/22/12 6:51 PM 130 2/23/12 1:01 PM 187

2/22/12 11:42 AM 191 2/22/12 6:52 PM 129 2/23/12 1:02 PM 186

2/22/12 11:43 AM 191 2/22/12 6:53 PM 129 2/23/12 1:03 PM 184

2/22/12 11:44 AM 191 2/22/12 6:54 PM 129 2/23/12 1:04 PM 184

2/22/12 11:45 AM 191 2/22/12 6:55 PM 130 2/23/12 1:05 PM 183

2/22/12 11:46 AM 192 2/22/12 6:56 PM 132 2/23/12 1:06 PM 182

2/22/12 11:47 AM 193 2/22/12 6:57 PM 133 2/23/12 1:07 PM 182

2/22/12 11:48 AM 193 2/22/12 6:58 PM 135 2/23/12 1:08 PM 181

2/22/12 11:49 AM 194 2/22/12 6:59 PM 136 2/23/12 1:09 PM 180

2/22/12 11:50 AM 194 2/22/12 7:00 PM 138 2/23/12 1:10 PM 180

2/22/12 11:51 AM 195 2/22/12 7:01 PM 140 2/23/12 1:11 PM 179

2/22/12 11:52 AM 196 2/22/12 7:02 PM 141 2/23/12 1:12 PM 179

2/22/12 11:53 AM 196 2/22/12 7:03 PM 143 2/23/12 1:13 PM 179

2/22/12 11:54 AM 197 2/22/12 7:04 PM 144 2/23/12 1:14 PM 178

2/22/12 11:55 AM 198 2/22/12 7:05 PM 145 2/23/12 1:15 PM 178

2/22/12 11:56 AM 199 2/22/12 7:06 PM 146 2/23/12 1:16 PM 178

2/22/12 11:57 AM 199 2/22/12 7:07 PM 146 2/23/12 1:17 PM 178

2/22/12 11:58 AM 200 2/22/12 7:08 PM 147 2/23/12 1:18 PM 178

2/22/12 11:59 AM 200 2/22/12 7:09 PM 147 2/23/12 1:19 PM 178

2/22/12 12:00 PM 201 2/22/12 7:10 PM 148 2/23/12 1:20 PM 178

2/22/12 12:01 PM 202 2/22/12 7:11 PM 148 2/23/12 1:21 PM 180

2/22/12 12:02 PM 202 2/22/12 7:12 PM 148 2/23/12 1:22 PM 183

2/22/12 12:03 PM 203 2/22/12 7:13 PM 149 2/23/12 1:23 PM 186

2/22/12 12:04 PM 204 2/22/12 7:14 PM 150 2/23/12 1:24 PM 188

2/22/12 12:05 PM 204 2/22/12 7:15 PM 150 2/23/12 1:25 PM 191

2/22/12 12:06 PM 205 2/22/12 7:16 PM 151 2/23/12 1:26 PM 195

2/22/12 12:07 PM 206 2/22/12 7:17 PM 151 2/23/12 1:27 PM 198

2/22/12 12:08 PM 207 2/22/12 7:18 PM 151 2/23/12 1:28 PM 200

2/22/12 12:09 PM 207 2/22/12 7:19 PM 150 2/23/12 1:29 PM 204

2/22/12 12:10 PM 208 2/22/12 7:20 PM 149 2/23/12 1:30 PM 206

2/22/12 12:11 PM 208 2/22/12 7:21 PM 147 2/23/12 1:31 PM 208

2/22/12 12:12 PM 209 2/22/12 7:22 PM 145 2/23/12 1:32 PM 210

2/22/12 12:13 PM 210 2/22/12 7:23 PM 143 2/23/12 1:33 PM 212

2/22/12 12:14 PM 210 2/22/12 7:24 PM 142 2/23/12 1:34 PM 213
Bag House #5 Inlet Temperatures (°F) Test 1 Test 2 Test 3 Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average

2/22/12 12:15 PM 211 2/22/12 7:25 PM 141 2/23/12 1:35 PM 215

2/22/12 12:16 PM 211 2/22/12 7:26 PM 141 2/23/12 1:36 PM 215

2/22/12 12:17 PM 211 2/22/12 7:27 PM 141 2/23/12 1:37 PM 216

2/22/12 12:18 PM 211 2/22/12 7:28 PM 142 2/23/12 1:38 PM 217

2/22/12 12:19 PM 212 2/22/12 7:29 PM 142 2/23/12 1:39 PM 218

2/22/12 12:20 PM 212 2/22/12 7:30 PM 143 2/23/12 1:40 PM 219

2/22/12 12:21 PM 213 2/22/12 7:31 PM 144 2/23/12 1:41 PM 220

2/22/12 12:22 PM 213 2/22/12 7:32 PM 144 2/23/12 1:42 PM 220

2/22/12 12:23 PM 213 2/22/12 7:33 PM 145 2/23/12 1:43 PM 221

2/22/12 12:24 PM 213 2/22/12 7:34 PM 146 2/23/12 1:44 PM 221

2/22/12 12:25 PM 214 2/22/12 7:35 PM 147 2/23/12 1:45 PM 222

2/22/12 12:26 PM 214 2/22/12 7:36 PM 148 2/23/12 1:46 PM 222

2/22/12 12:27 PM 214 2/22/12 7:37 PM 148 2/23/12 1:47 PM 223

2/22/12 12:28 PM 214 2/22/12 7:38 PM 149 2/23/12 1:48 PM 224

2/22/12 12:29 PM 214 2/22/12 7:39 PM 149 2/23/12 1:49 PM 224

2/22/12 12:30 PM 214 2/22/12 7:40 PM 150 2/23/12 1:50 PM 224

2/22/12 12:31 PM 214 2/22/12 7:41 PM 150 2/23/12 1:51 PM 223

2/22/12 12:32 PM 214 2/22/12 7:42 PM 151 2/23/12 1:52 PM 223

2/22/12 12:33 PM 215 2/22/12 7:43 PM 151 2/23/12 1:53 PM 223

2/22/12 12:34 PM 215 2/22/12 7:44 PM 152 2/23/12 1:54 PM 222

2/22/12 12:35 PM 215 2/22/12 7:45 PM 152 2/23/12 1:55 PM 222

2/22/12 12:36 PM 215 2/22/12 7:46 PM 153 2/23/12 1:56 PM 222

2/22/12 12:37 PM 215 2/22/12 7:47 PM 153 2/23/12 1:57 PM 221

2/22/12 12:38 PM 215 2/22/12 7:48 PM 154 2/23/12 1:58 PM 221

2/22/12 12:39 PM 216 2/22/12 7:49 PM 154 2/23/12 1:59 PM 220

2/22/12 12:40 PM 216 2/22/12 7:50 PM 155 2/23/12 2:00 PM 219

2/22/12 12:41 PM 216 2/22/12 7:51 PM 154 2/23/12 2:01 PM 218

2/22/12 12:42 PM 216 2/22/12 7:52 PM 154 2/23/12 2:02 PM 218

2/22/12 12:43 PM 216 2/22/12 7:53 PM 152 2/23/12 2:03 PM 219

2/22/12 12:44 PM 216 2/22/12 7:54 PM 150 2/23/12 2:04 PM 219

2/22/12 12:45 PM 216 2/22/12 7:55 PM 147 2/23/12 2:05 PM 219

2/22/12 12:46 PM 216 2/22/12 7:56 PM 145 2/23/12 2:06 PM 220

2/22/12 12:47 PM 216 2/22/12 7:57 PM 143 2/23/12 2:07 PM 220

2/22/12 12:48 PM 216 2/22/12 7:58 PM 141 2/23/12 2:08 PM 220

2/22/12 12:49 PM 216 2/22/12 7:59 PM 140 2/23/12 2:09 PM 220

2/22/12 12:50 PM 216 2/22/12 8:00 PM 139 2/23/12 2:10 PM 221

2/22/12 12:51 PM 215 2/22/12 8:01 PM 139 2/23/12 2:11 PM 221

2/22/12 12:52 PM 215 2/22/12 8:02 PM 139 2/23/12 2:12 PM 222

2/22/12 12:53 PM 215 2/22/12 8:03 PM 140 2/23/12 2:13 PM 222

2/22/12 12:54 PM 214 2/22/12 8:04 PM 140 2/23/12 2:14 PM 223

2/22/12 12:55 PM 214 2/22/12 8:05 PM 141 2/23/12 2:15 PM 224

2/22/12 12:56 PM 2/22/12 12:56 PM 214 2/22/12 8:06 PM 2/22/12 8:06 PM 142 2/23/12 2:16 PM 2/23/12 2:16 PM 224

2/22/12 12:57 PM 213 2/22/12 8:07 PM 142 2/23/12 2:17 PM 224

2/22/12 12:58 PM 213 2/22/12 8:08 PM 143 2/23/12 2:18 PM 225

2/22/12 12:59 PM 212 2/22/12 8:09 PM 143 2/23/12 2:19 PM 225

2/22/12 1:00 PM 211 2/22/12 8:10 PM 144 2/23/12 2:20 PM 225

2/22/12 1:01 PM 210 2/22/12 8:11 PM 145 2/23/12 2:21 PM 225

2/22/12 1:02 PM 207 2/22/12 8:12 PM 145 2/23/12 2:22 PM 225

2/22/12 1:03 PM 205 2/22/12 8:13 PM 146 2/23/12 2:23 PM 226

2/22/12 1:04 PM 202 2/22/12 8:14 PM 145 2/23/12 2:24 PM 226

2/22/12 1:05 PM 200 2/22/12 8:15 PM 144 2/23/12 2:25 PM 226

2/22/12 1:06 PM 198 2/22/12 8:16 PM 143 2/23/12 2:26 PM 226

2/22/12 1:07 PM 196 2/22/12 8:17 PM 141 2/23/12 2:27 PM 226

2/22/12 1:08 PM 194 2/22/12 8:18 PM 139 2/23/12 2:28 PM 227

2/22/12 1:09 PM 192 2/22/12 8:19 PM 137 2/23/12 2:29 PM 227

2/22/12 1:10 PM 190 2/22/12 8:20 PM 135 2/23/12 2:30 PM 227

2/22/12 1:11 PM 188 2/22/12 8:21 PM 133 2/23/12 2:31 PM 228

2/22/12 1:12 PM 187 2/22/12 8:22 PM 131 2/23/12 2:32 PM 228

2/22/12 1:13 PM 185 2/22/12 8:23 PM 129 2/23/12 2:33 PM 226

2/22/12 1:14 PM 184 2/22/12 8:24 PM 127 2/23/12 2:34 PM 225

2/22/12 1:15 PM 184 2/22/12 8:25 PM 127 2/23/12 2:35 PM 222

2/22/12 1:16 PM 182 2/22/12 8:26 PM 127 2/23/12 2:36 PM 219

2/22/12 1:17 PM 181 2/22/12 8:27 PM 128 2/23/12 2:37 PM 217

2/22/12 1:18 PM 180 2/22/12 8:28 PM 128 2/23/12 2:38 PM 214

2/22/12 1:19 PM 179 2/22/12 8:29 PM 129 2/23/12 2:39 PM 212

2/22/12 1:20 PM 178 2/22/12 8:30 PM 130 2/23/12 2:40 PM 210

2/22/12 1:21 PM 177 2/22/12 8:31 PM 131 2/23/12 2:41 PM 207

2/22/12 1:22 PM 176 2/22/12 8:32 PM 132 2/23/12 2:42 PM 206

2/22/12 1:23 PM 175 2/22/12 8:33 PM 133 2/23/12 2:43 PM 204

2/22/12 1:24 PM 174 2/22/12 8:34 PM 133 2/23/12 2:44 PM 202

2/22/12 1:25 PM 174 2/22/12 8:35 PM 133 2/23/12 2:45 PM 201

2/22/12 1:26 PM 173 2/22/12 8:36 PM 132 2/23/12 2:46 PM 200

2/22/12 1:27 PM 172 2/22/12 8:37 PM 131 2/23/12 2:47 PM 199

2/22/12 1:28 PM 172 2/22/12 8:38 PM 130 2/23/12 2:48 PM 198

2/22/12 1:29 PM 172 2/22/12 8:39 PM 128 2/23/12 2:49 PM 198

2/22/12 1:30 PM 171 2/22/12 8:40 PM 127 2/23/12 2:50 PM 197

2/22/12 1:31 PM 171 2/22/12 8:41 PM 126 2/23/12 2:51 PM 196

2/22/12 1:32 PM 171 2/22/12 8:42 PM 124 2/23/12 2:52 PM 196

2/22/12 1:33 PM 170 2/22/12 8:43 PM 123 2/23/12 2:53 PM 195

2/22/12 1:34 PM 170 2/22/12 8:44 PM 122 2/23/12 2:54 PM 194

2/22/12 1:35 PM 169 2/22/12 8:45 PM 120 2/23/12 2:55 PM 193

2/22/12 1:36 PM 169 2/22/12 8:46 PM 119 2/23/12 2:56 PM 193

2/22/12 1:37 PM 169 2/22/12 8:47 PM 119 2/23/12 2:57 PM 193

2/22/12 1:38 PM 168 2/22/12 8:48 PM 118 2/23/12 2:58 PM 192

2/22/12 1:39 PM 168 2/22/12 8:49 PM 117 2/23/12 2:59 PM 191
Bag House #5 Inlet Temperatures (°F) Test 1 Test 2 Test 3 Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average

2/22/12 1:40 PM 167 2/22/12 8:50 PM 117 2/23/12 3:00 PM 190

2/22/12 1:41 PM 167 2/22/12 8:51 PM 116 2/23/12 3:01 PM 190

2/22/12 1:42 PM 167 2/22/12 8:52 PM 116 2/23/12 3:02 PM 189

2/22/12 1:43 PM 166 2/22/12 8:53 PM 116 2/23/12 3:03 PM 189

2/22/12 1:44 PM 166 2/22/12 8:54 PM 115 2/23/12 3:04 PM 189

2/22/12 1:45 PM 166 2/22/12 8:55 PM 115 2/23/12 3:05 PM 188

2/22/12 1:46 PM 165 2/22/12 8:56 PM 115 2/23/12 3:06 PM 188

2/22/12 1:47 PM 165 2/22/12 8:57 PM 114 2/23/12 3:07 PM 187

2/22/12 1:48 PM 165 2/22/12 8:58 PM 114 2/23/12 3:08 PM 186

2/22/12 1:49 PM 165 2/22/12 8:59 PM 114 2/23/12 3:09 PM 186

2/22/12 1:50 PM 165 2/22/12 9:00 PM 114 2/23/12 3:10 PM 185

2/22/12 1:51 PM 165 2/22/12 9:01 PM 113 2/23/12 3:11 PM 185

2/22/12 1:52 PM 165 2/22/12 9:02 PM 113 2/23/12 3:12 PM 185

2/22/12 1:53 PM 165 2/22/12 9:03 PM 113 2/23/12 3:13 PM 184

2/22/12 1:54 PM 165 2/22/12 9:04 PM 113 2/23/12 3:14 PM 182

2/22/12 1:55 PM 165 2/22/12 9:05 PM 113 2/23/12 3:15 PM 180

2/22/12 1:56 PM 165 2/22/12 9:06 PM 114 2/23/12 3:16 PM 177

2/22/12 1:57 PM 165 2/22/12 9:07 PM 115 2/23/12 3:17 PM 175

2/22/12 1:58 PM 166 2/22/12 9:08 PM 118 2/23/12 3:18 PM 171

2/22/12 1:59 PM 166 2/22/12 9:09 PM 120 2/23/12 3:19 PM 169

2/22/12 2:00 PM 166 2/22/12 9:10 PM 122 2/23/12 3:20 PM 166

2/22/12 2:01 PM 166 2/22/12 9:11 PM 122 2/23/12 3:21 PM 163

2/22/12 2:02 PM 166 2/22/12 9:12 PM 122 2/23/12 3:22 PM 160

2/22/12 2:03 PM 166 2/22/12 9:13 PM 122 2/23/12 3:23 PM 158

2/22/12 2:04 PM 166 2/22/12 9:14 PM 121 2/23/12 3:24 PM 155

2/22/12 2:05 PM 165 2/22/12 9:15 PM 120 2/23/12 3:25 PM 153

2/22/12 2:06 PM 165 2/22/12 9:16 PM 120 2/23/12 3:26 PM 151

2/22/12 2:07 PM 165 2/22/12 9:17 PM 119 2/23/12 3:27 PM 149

2/22/12 2:08 PM 165 2/22/12 9:18 PM 118 2/23/12 3:28 PM 147

2/22/12 2:09 PM 165 2/22/12 9:19 PM 117 2/23/12 3:29 PM 146

2/22/12 2:10 PM 166 2/22/12 9:20 PM 117 2/23/12 3:30 PM 144

2/22/12 2:11 PM 166 2/22/12 9:21 PM 116

2/22/12 2:12 PM 166 2/22/12 9:22 PM 116

2/22/12 2:13 PM 166 2/22/12 9:23 PM 115

2/22/12 2:14 PM 166 2/22/12 9:24 PM 115

2/22/12 2:15 PM 166 2/22/12 9:25 PM 114

2/22/12 2:16 PM 166 2/22/12 9:26 PM 114

2/22/12 2:17 PM 166 2/22/12 9:27 PM 113

2/22/12 2:18 PM 166 2/22/12 9:28 PM 113

2/22/12 2:19 PM 166 2/22/12 9:29 PM 112

2/22/12 2:20 PM 166 2/22/12 9:30 PM 112

2/22/12 2:21 PM 165 2/22/12 9:31 PM 112

2/22/12 2:22 PM 164 2/22/12 9:32 PM 111

2/22/12 2:23 PM 162 2/22/12 9:33 PM 111

2/22/12 2:24 PM 160 2/22/12 9:34 PM 111

2/22/12 2:25 PM 157 2/22/12 9:35 PM 110

2/22/12 2:26 PM 155 2/22/12 9:36 PM 110

2/22/12 2:27 PM 152 2/22/12 9:37 PM 110

2/22/12 2:28 PM 149 2/22/12 9:38 PM 110

2/22/12 2:29 PM 147 2/22/12 9:39 PM 110

2/22/12 2:30 PM 144 2/22/12 9:40 PM 110

2/22/12 2:31 PM 142 2/22/12 9:41 PM 110

2/22/12 2:32 PM 140 2/22/12 9:42 PM 109

2/22/12 2:33 PM 138 2/22/12 9:43 PM 109

2/22/12 2:34 PM 136 2/22/12 9:44 PM 109

2/22/12 2:35 PM 134 2/22/12 9:45 PM 109

2/22/12 2:36 PM 132 2/22/12 9:46 PM 109

2/22/12 2:37 PM 131 2/22/12 9:47 PM 109

2/22/12 2:38 PM 130 2/22/12 9:48 PM 109

2/22/12 2:39 PM 129 2/22/12 9:49 PM 108

2/22/12 2:40 PM 128 2/22/12 9:50 PM 108

2/22/12 9:51 PM 108

2/22/12 9:52 PM 108

2/22/12 9:53 PM 108

2/22/12 9:54 PM 108

2/22/12 9:55 PM 107

2/22/12 9:56 PM 107

2/22/12 9:57 PM 107

2/22/12 9:58 PM 107

2/22/12 9:59 PM 107

2/22/12 10:00 PM 107

2/22/12 10:01 PM 107

2/22/12 10:02 PM 106

2/22/12 10:03 PM 106

2/22/12 10:04 PM 106

2/22/12 10:05 PM 106

2/22/12 10:06 PM 106

2/22/12 10:07 PM 106

2/22/12 10:08 PM 106

2/22/12 10:09 PM 106

2/22/12 10:10 PM 106

2/22/12 10:11 PM 106

2/22/12 10:12 PM 106

2/22/12 10:13 PM 106

2/22/12 10:14 PM 106
Bag House #5 Inlet Temperatures (°F) Test 1 Test 2 Test 3 Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average Data Link Average One Minute Samples

Samples

Average

2/22/12 10:15 PM 106

2/22/12 10:16 PM 106

2/22/12 10:17 PM 106

2/22/12 10:18 PM 106

2/22/12 10:19 PM 106

2/22/12 10:20 PM 106