# Aluminum Chip Dryer ICR Emissions Test Report

Prepared for:


# General Motors LLC

Bedford, Indiana

General Motors LLC
Bedford PowerTrain
105 GM Drive Bedford, Indiana 47421

Project No. 10-3997.00 October 7, 2010

BT Environmental Consulting, Inc.
2615 Wolcott Street Ferndale, Michigan 48220 (248) 548-8070

## Executive Summary

BT Environmental Consulting, Inc. (BTEC) was retained by General Motors LLC – Bedford Castings, Engines, Transmissions and Components (GM) to evaluate air pollutant emissions rates from a single exhaust stack associated with the Thermal Aluminum Chip Dryer located at the GM Facility located in Bedford, IN. The test pr ogram consisted of the following parameters;

• 

## Exhaust gas flowrates an d moisture content,

• 

## Exhaust gas oxygen (O 2 

## ) and carbon dioxide (CO 2 

## ) concentrations,

• 

## Total hydrocarbons (THC) concentrations,

• 

## Exhaust gas volatile and semi-volatile organic hazardous air pollutant (HAP) concentrations

Testing for this project was conducted on August 23 rd 

## and 24 th 

## , 2010. The emissions test program was requested in a letter sent to GM by the Un ited States Environmental Protection Agency (U.S. EPA) pursuant to U.S. EPA authority under Section 114 of the Clean Air Act.

Testing consisted of triplicate test runs of approximately 180-minutes for each compound. Sampling was performed utilizing United States Environmental Protection Agency (U.S. EPA) methods. The average results of the testing are highlighted in the following table:

Table I Overall Emission Summary

Test Run Process Weight Rate (lb/hr) Total Hydrocarbons (kg/hr) Speciated SemiVolatile Organic HAPs (kg/hr) Process Weight Rate (lb/hr) Speciated Volatile Organic

HAPs (kg/hr) O2 (%) CO2 (%)

1 11,850 0.671 0.000132 11,849 0.0012 16.2 2.5

2 11,877 0.627 0.0000273 11,875 0.0011 16.2 3.1

3 11,350 0.119 0.0000445 11,360 0.00094 16.6 2.4

Average 11,692 0.472 0.0000678 11,695 0.0011 16.3 2.7

Test Run Process Weight Rate (Mg/hr) Total Hydrocarbons (kg/Mg of feed) Speciated SemiVolatile Organic HAPs (kg/Mg of feed) Process Weight Rate (Mg/hr) Speciated Volatile Organic

HAPs (kg/Mg of feed)

1 5.38 0.125 0.0000245 5.37 0.00022

2 5.39 0.116 0.00000508 5.39 0.00020

3 5.15 0.023 0.00000865 5.15 0.00018 Average 5.31 0.088 0.0000127 5.30 0.00020

1: See Table 3 for individual Volatile Organic HAP emissions 2: See Table 4 for individual Se mi-Volatile Organic HAP emissions



## General Motors LLC BTEC Project No. 10-3997.00 Aluminum Chip Dryer ICR Emissions Test Report Oct ober 7, 2010 

## i

## General Motors LLC BTEC Project No. 10-3997.00 Aluminum Chip Dryer ICR Emissions Test Report Oct ober 7, 2010 

## ii TABLE OF CONTENTS

1.0 INTRODUCTION ............................................................................................................... 1

2.0 PROCESS DESCRIPTION ............................................................................................... 1

3.0 SAMPLING AND ANALYTICAL METHODOLOGIES .............................................. 2

3.1 E XHAUST 

## G AS 

## V ELOCITY AND 

## M OISTURE 

## C ONTENT 

## ......................................................... 2

3.2 O XYGEN AND 

## C ARBON 

## D IOXIDE 

## (USEPA M ETHOD 

## 3A) .................................................... 3

3.3 T OTAL 

## H YDROCARBONS 

## (USEPA M ETHOD 

## 25A) .............................................................. 3

3.4 S EMI 

## V OLATILE 

## O RGANIC 

## HAP S 

## (M ETHOD 

## 0010) ............................................................. 3

3.5 V OLATILE 

## O RGANIC 

## HAP S 

## (M ETHOD 

## 0031)...................................................................... 4

4.0 TEST RESULTS ................................................................................................................. 5

TABLES

Table 1 – Overall Emissions Summary Table 2 – Aluminum Chip Dryer THC Emission Rates Table 3 – Aluminum Chip Dryer Volatile Organic HAP Emission Test Results Summary Table 4 – Aluminum Chip Dryer Semi-Volatil e Organic HAP Emission Test Results Summary

FIGURES

Figure 1 – Aluminum Chip Dryer Exha ust Stack Traverse Point Diagram Figure 2 – USEPA Method 3A Sampling Train Diagram Figure 3 – USEPA Method 25A Sampling Train Diagram Figure 4 – USEPA Method 0010 Sampling Train Diagram Figure 5 – USEPA Method 0031 Sampling Train Diagram

APPENDICES

Appendix A – Field and Co mputer Generated Raw Data and Field Notes Appendix B – Calibration Data Appendix C – Raw CEM Data Appendix D – Laboratory Analytical Results Appendix E – Example Calculations Appendix F – Production Data Appendix G – Agency Communications Appendix H – USEPA ICR Reporting Tables

## 1.0 Introduction

BT Environmental Consulting, Inc. (BTEC) was retained by General Motors LLC – Bedford Castings, Engines, Transmissions and Components (GM) to evaluate air pollutant emissions rates from a single exhaust stack associated with the Thermal Aluminum Chip Dryer located at the GM Facility located in Bedford, IN. The test pr ogram consisted of the following parameters;

• 

## Exhaust gas flowrates an d moisture content,

• 

## Exhaust gas oxygen (O 2 

## ) and carbon dioxide (CO 2 

## ) concentrations,

• 

## Total hydrocarbons (THC) concentrations,

• 

## Exhaust gas volatile and semi-volatile organic hazardous air pollutant (HAP)

concentrations.

Testing for this project was conducted on August 23 rd 

## and 24th, 2010. The emissions test program was requested in a letter sent to GM by the Un ited States Environmental Protection Agency (U.S. EPA) pursuant to U.S. EPA authority under Section 114 of the Clean Air Act.

The following BTEC professionals participated in conducting this study: Todd Wessel and Jim Sharp, Senior Project Managers; Jeff Peitzsch and Dave Center, St aff Environmental Engineers; and Matthew Young, Environmental Technician. Mr . Jeffrey Hummel with GM provided on-site coordination for this project.

2.0 Process Description

As part of the die casting process, GM utilizes a natural gas-fired thermal aluminum chip dryer

to remove moisture and/or su rface impurities prior to charging th e dry aluminum chips into the plant’s melting furnaces. The maximum proce ss weight rate established by the initial performance testing in 2003 is 15,196 pounds/hour. The heat input rate resulting from natural gas consumption during the stack tests was a pproximately 9 MCF/hour. The aluminum chip dryer operation is controlled by th e following abatement equipment:

1. Cyclone Separator; 2. Afterburner/Oxidizer; and, 3. Baghouse

Dryer Drum Baghouse Afterburner/Oxidizer Cyclone Wet Chips

Dry Aluminum Chips Stack Exhaust

Sample Point



## General Motors LLC BTEC Project No. 10-3997.00 Aluminum Chip Dryer ICR Emissions Test Report Oct ober 7, 2010 1

## 3.0 Sampling and Analytical Methodologies

Sampling and analytical methodologies for the emissi ons test program can be separated into five categories as follows:

(1) Measurement of exhaust gas velocity and moisture content; (2) Measurement of exhaust gas oxygen (O 2 

## ) and carbon dioxide (CO 2 

## ) concentrations using the procedures of U.S. EPA Method 3A; (3) Measurement of exhaust gas total hydrocarbons (THC) concentrations and emission rates using U.S. EPA Method 25A; (4) Measurement of exhaust gas speciated semi -volatile organic HAPs concentrations and emission rates using Method 0010; and (5) Measurement of exhaust gas speciated vol atile organic HAPs concentrations and emission rates using Method 0031.

Descriptions of sampling and analytical met hodologies by category are su mmarized by Sections 3.1 through 3.5, respectively.

3.1 Exhaust Gas Velocity and Moisture Content

Measurement of exhaust gas velocity and mois ture content were conducted using the following reference test methods codified at Title 40, Part 60, Appendix A of the Code of Federal Regulations (40 CF R 60, Appendix A):

• Method 1 - “Sample and Velocity Trave rses for Stationary Sources”

• Method 2 - “Determination of Stack Gas Velo city and Volumetric Flowrate”

• Method 4 - “Determination of Moisture Content in Stack Gases”

Stack gas velocity traverses were conducted in accordance with the procedures outlined in Methods 1 and 2 (see Figure 1 for an exhaust stack tr averse point diagram). An S-type pitot tube with a thermocouple assembly, cal ibrated in accordance with Me thod 2, Section 4.1.1, was used to measure exhaust gas velocity pressures (using a manometer) a nd temperatures during testing. The S-type pitot tube dimensions were within sp ecified limits, therefore, a baseline pitot tube coefficient of 0.84 (dimensionless) was assigned.

A cyclonic flow check was performed at the samp ling location. The existence of cyclonic flow is determined by measuring the flow angle at each sample point. The flow angle is the angle

between the direction of flow and the axis of the stack. If the average of the absolute values of the flow angles is greater than 20 degrees, cyclonic flow exists. The null angle was determined to be less than 20 degree s at each sampling point.

Exhaust gas moisture content was evaluated usin g Method 4. Exhaust gas was extracted as part of the Method 0010 sampling train (see Figure 4 for schematics of the sampling train). Exhaust gas moisture content was then determined gravimetrically.

General Motors LLC BTEC Project No. 10-3997.00 Aluminum Chip Dryer ICR Emissions Test Report Oct ober 7, 2010 2

## 3.2 Oxygen and Carbon Dioxi de (USEPA Method 3A)

Exhaust gas O 2 

## and CO 2 

## concentrations were measured using the procedures of 40 CFR 60, Appendix A, Method 3A, “Determination of Oxygen and Carbon Dioxide Concentrations in Emissions from Stationary Sources” . The O 2 

## content of the gas stream was measured using a Teledyne paramagnetic O 2 

## gas analyzer. The CO 2 

## content of the gas stream was measured using a Teledyne infrared CO 2 

## gas analyzer. An integrated sa mple of the gas stream was drawn through an insulated stainless-steel probe with an in-line glass fiber filter to remove any particulate and into a tedlar sample bag utilizi ng an evacuated sample lung. At the completion of each test the gas sample was introduced to the analyzers. Data was recorded at 4-second intervals on a PC equipped with data acquisition software.

3.3 Total Hydrocarbons (USEPA Method 25A)

Total hydrocarbons (THC) concentrations were measured according to 40 CFR 60, Appendix A, Method 25A. A sample of the gas stream was draw n through a stainless steel probe with an inline glass fiber filter to remove a ny particulate, and a heated Teflon ® sample line to prevent the condensation of any moisture from the sample befo re it enters the analyzer. Data was recorded
at 4-second intervals on a PC equipped with IOtech ® II acquisition software. BTEC used a VIG Model 20 THC hydrocarbon analyzer to determine the THC concentration.

The VIG THC hydrocarbon analyzer channels a fr action of the gas sample through a capillary tube that directs the sample to the flame i onization detector (FID), where the hydrocarbons present in the sample are ionized into carbon. The carbon concentration is then determined by the detector in parts per million (ppm). This c oncentration is transmitted to the data acquisition system (DAS) at 4-second intervals in the form of an analog signal, sp ecifically voltage, to produce data that can be averaged over the durati on of the testing program. This data is then used to determine the average ppm for total hydr ocarbons (THC) using the equivalent units of propane (calibration gas). The analyzer wa s calibrated for a ra nge of 0 to 50 ppm.

In accordance with Method 25A, a 3-point (z ero, mid, and high) calibration check was performed on the THC analyzer. Calibration drift checks were performed at the completion of

each run.

3.4 Semi Volatile Organic HAPs (Method 0010)

Method 0010, was used to evaluate semi volatile organic HAP’s concentrations. The Method 0010 sampling train consisted of: (1 ) a stainless steel or borosilicat e glass nozzle, (2) a heated borosilicate or quartz probe liner; (2) a heated bo rosilicate or quartz glass filter holder containing a pre-weighed 90-mm quartz filter with Teflon f ilter support; (3) a condenser, (4) a sorbent trap, (5) an empty pot bellied impinger, (6) two Gr eenburg-Smith (GS) impingers each containing 100

ml of DI H 2 

## O, (7) an empty GS impinger, (8) a modified GS impinger containing a known weight of silica gel desiccant; (9) a length of sample line, an d (10) a Nutech control case equipped with a pump, dry gas meter, and calibrated orifice. Figure 4 provides an illustration of the Method 0010 sample train.

General Motors LLC BTEC Project No. 10-3997.00 Aluminum Chip Dryer ICR Emissions Test Report Oct ober 7, 2010 3

## After completion of the final leak test for each test run, the impinger train was carefully disassembled. The nozzle, probe, and front half of the filter housing were brushed and rinsed with a solvent mixture (1:1 v/v methanol/methyl ene chloride) and collected in a pre-cleaned glass sample container. The filter was recovere d and placed in its original Petri dish. The sorbent trap was removed and capped with para film. The liquid volume of the pot bellied impinger was measured gravimetrically and transfe rred to a glass sample container. The back half of the filter housing, the condenser, and pot bellied impinger were rinsed with the solvent mixture and the rinse was collected in a separa te glass sample container. The remaining impingers were gravimetrically analyzed for moisture gain and the liquid was discarded.

BTEC labeled each container with the test number, test location, and test date, and marked the level of liquid on the outside of th e container. In addition, blank samples of the solvent mixture, filter, and sorbent trap were collected. Sa mples were couriered by Maxxam personnel to the Maxxam laboratory for analysis.

3.5 Volatile Organic HAPs (Method 0031)

Exhaust gas volatile organic HAPs concentrations were measured using the procedures of Method 0031, “Sampling Method For Volati le Organic Compounds (SMVOC)” . The Method 0031 sampling train consisted of: (1) a heated borosilicate or quartz probe liner; (2) a three way glass/Teflon isolation valve, (3) a vertical conde nser, (4) two Tenax-GC so rbent traps in series, (5) a condensate trap, (6) anothe r vertical condenser, (7) an Anas orb-747 sorbent trap, (8) a small impinger containing a known weight of silica gel de siccant; (9) a length of sample line, and (10) a Nutech control case equipped w ith a pump, dry gas meter, and calibrated orifice. Figure 5 provides an illustration of the Method 0031 sample train.

The probe was placed at the center of the stack for non-isokinetic sampling. The sample train

was run for 40 minutes at a rate of 0.5 L/min at which point all the sorben t traps were recovered and replaced with new traps. A to tal of four sets of sorbent traps were used for each test for a total sample time of 160 minutes per test. The mass of liquid condensed in the condensate trap and silica gel impingers were measured gr avimetrically for moisture analysis.

BTEC labeled each trap with the test number, test location, and test date. In addition, blank samples of the sorbent traps we re collected. Samples were couriered by Maxxam personnel to the Maxxam laboratory for analysis.

General Motors LLC BTEC Project No. 10-3997.00 Aluminum Chip Dryer ICR Emissions Test Report Oct ober 7, 2010 4

## 4.0 Test Results

The results of the emissions test pr ogram are summarized by Table 1.

Table 1 Overall Emission Summary

Test Run Process Weight Rate (lb/hr) Total Hydrocarbons (kg/hr) Speciated SemiVolatile Organic HAPs (kg/hr) Process Weight Rate (lb/hr) Speciated Volatile Organic

HAPs (kg/hr) O 2 

## (%) CO 2 

## (%)

1 11,850 0.671 0.000132 11,849 0.0012 16.2 2.5

2 11,877 0.627 0.0000273 11,875 0.0011 16.2 3.1

3 11,350 0.119 0.0000445 11,360 0.00094 16.6 2.4

Average 11,692 0.472 0.0000678 11,695 0.0011 16.3 2.7

Test Run Process Weight Rate (Mg/hr) Total Hydrocarbons (kg/Mg of feed) Speciated SemiVolatile Organic HAPs (kg/Mg of feed) Process Weight Rate (Mg/hr) Speciated Volatile Organic

HAPs (kg/Mg of feed)

1 5.38 0.125 0.0000245 5.37 0.00022

2 5.39 0.116 0.00000508 5.39 0.00020

3 5.15 0.023 0.00000865 5.15 0.00018 Average 5.31 0.088 0.0000127 5.30 0.00020

1: See Table 3 for individual Volatile Organic HAP emissions 2: See Table 4 for individual Se mi-Volatile Organic HAP emissions



## Field and computer generated data for each test run are available in Appe ndix A, as well as all other applicable field data. Equipment calibra tion and span gas documentation is presented in Appendix B. Raw CEMs data is presented in Appendix C. Laborat ory analysis is available in Appendix D. Example calculations are available in Appendix E. Production data is available in Appendix F.

General Motors LLC BTEC Project No. 10-3997.00 Aluminum Chip Dryer ICR Emissions Test Report Oct ober 7, 2010 5

# TablesTable 2Aluminum Chip Dryer VOC Emission RatesGeneral Motors CorporationBedford FacilityBTEC Project No. 10-3997.00Sampling Dates: August 23rd and 24th, 2010ParameterRun 1 Run 2 Run 3 AverageTest Run Date 8/23/2010 8/24/2010 8/24/2010Test Run Time 16:49-20:06 7:47-11:05 11:52-15:08Outlet Flowrate (scfm) 16,076 16,168 15,88716,044Feed (lb/hr) 11,850 11,877 11,35011,692Outlet VOC Concentration (ppmv) 13.4 12.6 2.59.5Outlet VOC Concentration (ppmv, corrected as per USEPA 7E) 13.5 12.5 2.49.5VOC Emission Rate (kg/hr) 0.667 0.631 0.122 0.473VOC Emission Rate (kg/hr) (corrected as per USEPA 7E) 0.671 0.627 0.119 0.472VOC Emission Rate (kg/Mg of feed) 0.124 0.117 0.024 0.088VOC Emission Rate (kg/Mgof feed) (corrected as per USEPA 7E) 0.125 0.116 0.023 0.088Co= Average of initial and final zero gasesCma=Actual concentration of the calibration gasCm= Average of initial and final calibration gasesscfm = standard cubic feet per minuteppmv = parts per million on a volume-to-volume basislb/hr = pounds per hourMW = molecular weight (C3H8= 44.10)24.14 = molar volume of air at standard conditions (70oF, 29.92" Hg)35.31 = ft3per m3453600 = mg per lb453.6 = g per lb2.205 = lb per kg10^6 = g per MgEquationskg/hr = ppmv * MW/24.14 * 1/35.31 * 1/453,600 *scfm* 60 * 1/2.205kg/Mg of feed = kg/hr * 1/feed * 1/453.6 * 10^6Table 3 Aluminum Chip Dryer Volatile Organic HAP Emission Test Results Summary

GM Bedford BTEC Project No. 10-3997.00 Sampling Date: August 23-24, 2010

Parameter Run 1 Run 2 Run 3 Avera g e

Test Run Date 8/23/2010 8/24/2010 8/24/2010

Test Run Time 16:58-20:10 7:48-11:08 11:23-14:32

Exhaust Gas Flowrate (dscfm) 12,879 12,836 12,889 12,868 Sample Volume, Vmstd (dscf) 71.6 70.4 73.5 72

O 2 Concentration (%, Corrected as per Method 7E) 16.2 16.2 16.6 16.3

CO 2 Concentration (%, Corrected as per Method 7E) 2.5 3.1 2.4 2.7

Moisture % 0.59 0.67 0.64 1
Feed (lb/hr) 11,849 11,875 11,360 11,695

Laboratory Result (ug )

Miscellaneous Organic s 0.08 0.07 0.07 0.07 Trichlorofluoromethane (FREON 11 ) 1.64 1.63 1.63 1.63 1,1-Dichloroethylen e 0.92 0.89 0.89 0.90

Carbon Disulfid e 7.97 3.00 1.49 4.15 Methylene Chloride(Dichloromethan e 80.04 76.03 68.03 74.70
1,1-Dichloroethan e 0.36 0.35 0.35 0.35 trans-1,2-Dichloroethylen e 1.67 1.33 1.27 1.42

Chlorofor m 0.348 0.341 0.341 0.34
1,2-Dichloroethan e 0.44 0.43 0.43 0.43
1,1,1-Trichloroethan e 0.48 0.46 0.46 0.47

Carbon Tetrachlorid e 6.555 2.066 3.098 3.91

Benzen e 0.48 0.46 0.46 0.47
1,1,2-Trichloroethan e 0.44 0.43 0.43 0.43 1,2-Dichloropropan e 0.46 0.43 0.43 0.44 Trichloroethylen e 0.44 0.43 0.43 0.43

Dibromomethan e 0.62 0.57 0.54 0.58

Bromodichloromethan e 0.36 0.35 0.35 0.35 cis-1,3-Dichloropropen e 0.348 0.341 0.341 0.34 trans-1,3-Dichloropropen e 0.56 0.551 0.533 0.55

Dibromochloromethan e 0.58 0.41 0.52 0.50

Toluen e 0.92 1.42 1.38 1.24 Tetrachloroethylen e 1.31 0.8 0.87 0.99 Acrylonitril e 4.12 4.09 4.09 4.10 Chloropren e 0.8 0.8 0.8 0.80 Total Volatile Organic s 111.941 97.679 89.233 99.62

Emission Rates (kg/hr )

Miscellaneous Organic s 8.6E-07 7.7E-07 7.4E-07 7.9E-07 Trichlorofluoromethane (FREON 11 ) 1.8E-05 1.8E-05 1.7E-05 1.8E-05 1,1-Dichloroethylen e 9.9E-06 9.7E-06 9.4E-06 9.7E-06

Carbon Disulfide 8.6E-05 3.3E-05 1.6E-05 4.5E-05 Methylene Chloride(Dichloromethane) 8.6E-04 8.3E-04 7.2E-04 8.0E-04
1,1-Dichloroethane 3.9E-06 3.8E-06 3.7E-06 3.8E-06 trans-1,2-Dichloroethylene 1.8E-05 1.5E-05 1.3E-05 1.5E-05

Chloroform 3.8E-06 3.7E-06 3.6E-06 3.7E-06
1,2-Dichloroethane 4.7E-06 4.7E-06 4.5E-06 4.7E-06
1,1,1-Trichloroethane 5.2E-06 5.0E-06 4.8E-06 5.0E-06

Carbon Tetrachloride 7.1E-05 2.3E-05 3.3E-05 4.2E-05

Benzene 5.2E-06 5.0E-06 4.8E-06 5.0E-06
1,1,2-Trichloroethane 4.7E-06 4.7E-06 4.5E-06 4.7E-06 1,2-Dichloropropane 5.0E-06 4.7E-06 4.5E-06 4.7E-06 Trichloroethylene 4.7E-06 4.7E-06 4.5E-06 4.7E-06

Dibromomethane 6.7E-06 6.2E-06 5.7E-06 6.2E-06

Bromodichloromethane 3.9E-06 3.8E-06 3.7E-06 3.8E-06 cis-1,3-Dichloropropene 3.8E-06 3.7E-06 3.6E-06 3.7E-06 trans-1,3-Dichloropropene 6.0E-06 6.0E-06 5.6E-06 5.9E-06

Dibromochloromethane 6.3E-06 4.5E-06 5.5E-06 5.4E-06

Toluene 9.9E-06 1.6E-05 1.5E-05 1.3E-05 Tetrachloroethylen e 1.4E-05 8.8E-06 9.2E-06 1.1E-05
Acrylonitrile 4.4E-05 4.5E-05 4.3E-05 4.4E-05 Chloroprene 8.6E-06 8.8E-06 8.4E-06 8.6E-06 Total Volatile Organics 1.2E-03 1.1E-03 9.4E-04 1.1E-03

Emission Rates (kg/Mg of feed )

Miscellaneous Organic s 1.6E-07 1.4E-07 1.4E-07 1.5E-07 Trichlorofluoromethane (FREON 11 ) 3.3E-06 3.3E-06 3.3E-06 3.3E-06 1,1-Dichloroethylen e 1.8E-06 1.8E-06 1.8E-06 1.8E-06

Carbon Disulfid e 1.6E-05 6.1E-06 3.0E-06 8.4E-06 Methylene Chloride(Dichloromethan e 1.6E-04 1.5E-04 1.4E-04 1.5E-04
1,1-Dichloroethan e 7.2E-07 7.1E-07 7.1E-07 7.2E-07 trans-1,2-Dichloroethylen e 3.4E-06 2.7E-06 2.6E-06 2.9E-06

Chlorofor m 7.0E-07 6.9E-07 7.0E-07 7.0E-07
1,2-Dichloroethan e 8.8E-07 8.7E-07 8.8E-07 8.8E-07
1,1,1-Trichloroethan e 9.6E-07 9.3E-07 9.4E-07 9.5E-07

Carbon Tetrachlorid e 1.3E-05 4.2E-06 6.3E-06 7.9E-06

Benzen e 9.6E-07 9.3E-07 9.4E-07 9.5E-07
1,1,2-Trichloroethan e 8.8E-07 8.7E-07 8.8E-07 8.8E-07 1,2-Dichloropropan e 9.2E-07 8.7E-07 8.8E-07 8.9E-07 Trichloroethylen e 8.8E-07 8.7E-07 8.8E-07 8.8E-07

Dibromomethan e 1.2E-06 1.2E-06 1.1E-06 1.2E-06

Bromodichloromethan e 7.2E-07 7.1E-07 7.1E-07 7.2E-07 cis-1,3-Dichloropropen e 7.0E-07 6.9E-07 7.0E-07 7.0E-07 trans-1,3-Dichloropropen e 1.1E-06 1.1E-06 1.1E-06 1.1E-06

Dibromochloromethan e 1.2E-06 8.3E-07 1.1E-06 1.0E-06

Toluen e 1.8E-06 2.9E-06 2.8E-06 2.5E-06 Tetrachloroethylen e 2.6E-06 1.6E-06 1.8E-06 2.0E-06 Acrylonitril e 8.3E-06 8.3E-06 8.3E-06 8.3E-06 Chloropren e 1.6E-06 1.6E-06 1.6E-06 1.6E-06 Total Volatile Organic s 2.2E-04 2.0E-04 1.8E-04 2.0E-04

dscf = dry standard cubic feet kg/hr = kilograms per hour kg/Mg of feed = kilograms of pollutant per Megagram of feed 31.31 = Ft^3 per m^3 453.6 = grams per pound 10^6 = g per Mg 10^9 = ug per kg

All results not in bold are flagged as BDL. DL used for calculations All results in bold are flagged detection level limited (DLL). Fractions with results below DL use DL for calculations. No results flagged as ADL.

equations: kg/hr = pollutant(ug) * (1/10^9) * (1/Vstd) * dscfm * 60 kg/Mg of feed = kg/hr / feed * (1/453.6) * 10^6Table 4
Aluminum Chip Dryer Semi-Volatile Organic HAP Emission Test Results Summary

GM Bedford
BTEC Project No. 10-3997.00
Sampling Date: August 23-24, 2010

Parameter Run 1 Run 2 Run 3 Average

Test Run Date 8/23/2010 8/24/2010 8/24/2010

Test Run Time 16:49-20:06 7:47-11:05 11:52-15:08

Exhaust Gas Flowrate (dscfm) 12,879 12,836 12,889 12,868 Sample Volume, Vmstd (dscf) 156.5 158.3 157.7 157

O 2 Concentration (%, Corrected as per Method 7E) 16.2 16.2 16.6 16.3

CO 2 Concentration (%, Corrected as per Method 7E) 2.5 3.1 2.4 2.7

Moisture % 18.87 20.61 19.89 20
Feed (lb/hr) 11,850 11,877 11,350 11,692

Laboratory Result (ug)

A cenaphthen e 0.36 0.10 0.10 0.19

A cenaphthylen e 0.10 0.10 0.10 0.10

A nthracen e 0.30 0.10 0.10 0.17 Benzo(a)anthracen e 0.10 0.10 0.10 0.10 Benzo(a)pyren e 0.10 0.10 0.10 0.10 Benzo(b)fluoranthen e 0.10 0.10 0.10 0.10 Benzo(g,h,i)perylen e 0.10 0.10 0.10 0.10 Benzo(k)fluoranthen e 0.10 0.10 0.10 0.10 Chrysen e 0.10 0.10 0.10 0.10 Dibenz(a,h)anthracen e 0.10 0.10 0.10 0.10

Fluoranthen e 0.38 0.23 0.10 0.24

Fluoren e 1.70 0.21 0.10 0.67 Indeno(1,2,3-cd)pyren e 0.10 0.10 0.10 0.10 Naphthalen e 18.50 3.12 7.24 9.62

Phenanthren e 4.39 0.65 0.44 1.83 Pyren e 0.10 0.31 0.10 0.17 Total Semi-Volatile Organic s 26.63 5.62 9.08 13.78

Emission Rates (kg/hr)

A cenaphthen e 1.78E-06 4.87E-07 4.90E-07 9.2E-07

A cenaphthylen e 4.94E-07 4.87E-07 4.90E-07 4.9E-07

A nthracen e 1.48E-06 4.87E-07 4.90E-07 8.2E-07 Benzo(a)anthracene 4.94E-07 4.87E-07 4.90E-07 4.9E-07 Benzo(a)pyrene 4.94E-07 4.87E-07 4.90E-07 4.9E-07 Benzo(b)fluoranthene 4.94E-07 4.87E-07 4.90E-07 4.9E-07 Benzo(g,h,i)perylene 4.94E-07 4.87E-07 4.90E-07 4.9E-07 Benzo(k)fluoranthene 4.94E-07 4.87E-07 4.90E-07 4.9E-07 Chrysene 4.94E-07 4.87E-07 4.90E-07 4.9E-07 Dibenz(a,h)anthracene 4.94E-07 4.87E-07 4.90E-07 4.9E-07

Fluoranthene 1.88E-06 1.12E-06 4.90E-07 1.2E-06

Fluorene 8.40E-06 1.02E-06 4.90E-07 3.3E-06 Indeno(1,2,3-cd)pyrene 4.94E-07 4.87E-07 4.90E-07 4.9E-07 Naphthalene 9.14E-05 1.52E-05 3.55E-05 4.7E-05

Phenanthrene 2.17E-05 3.16E-06 2.16E-06 9.0E-06 Pyrene 4.94E-07 1.51E-06 4.90E-07 8.3E-07 Total Volatile Organics 1.32E-04 2.73E-05 4.45E-05 6.78E-05

Emission Rates (kg/Mg of feed)

A cenaphthen e 3.31E-07 9.03E-08 9.52E-08 1.7E-07

A cenaphthylen e 9.19E-08 9.03E-08 9.52E-08 9.2E-08

A nthracen e 2.76E-07 9.03E-08 9.52E-08 1.5E-07 Benzo(a)anthracen e 9.19E-08 9.03E-08 9.52E-08 9.2E-08 Benzo(a)pyren e 9.19E-08 9.03E-08 9.52E-08 9.2E-08 Benzo(b)fluoranthen e 9.19E-08 9.03E-08 9.52E-08 9.2E-08 Benzo(g,h,i)perylen e 9.19E-08 9.03E-08 9.52E-08 9.2E-08 Benzo(k)fluoranthen e 9.19E-08 9.03E-08 9.52E-08 9.2E-08 Chrysen e 9.19E-08 9.03E-08 9.52E-08 9.2E-08 Dibenz(a,h)anthracen e 9.19E-08 9.03E-08 9.52E-08 9.2E-08

Fluoranthen e 3.49E-07 2.08E-07 9.52E-08 2.2E-07

Fluoren e 1.56E-06 1.90E-07 9.52E-08 6.2E-07 Indeno(1,2,3-cd)pyren e 9.19E-08 9.03E-08 9.52E-08 9.2E-08 Naphthalen e 1.70E-05 2.82E-06 6.89E-06 8.9E-06

Phenanthren e 4.03E-06 5.87E-07 4.19E-07 1.7E-06 Pyren e 9.19E-08 2.80E-07 9.52E-08 1.6E-07 Total Volatile Organic s 2.45E-05 5.08E-06 8.65E-06 1.27E-05

dscf = dry standard cubic feet kg/hr = kilograms per hour kg/Mg of feed = kilograms of pollutant per Megagram of feed
31.31 = Ft^3 per m^3 453.6 = grams per pound
10^6 = g per Mg 10^9 = ug per kg

All results not in bold are flagged as BDL. DL used for calculations All results in bold are flagged below detection limit (BDL). Fractions with results below DL use DL for calculations. No results flagged as ADL.

equations: kg/hr = pollutant(ug) * (1/10^9) * (1/Vstd) * dscfm * 60 kg/Mg of feed = kg/hr / feed * (1/453.6) * 10^6

# Figures

### diameter = 60 inches

Points Distance "

1 1.26

2 4.02

3 7.08

4 10.62

5 15.00

6 21.36

7 30.64

8 45.00

9 49.38

10 52.92

11 55.98

12 58.74



## Figure No. 1

Site: Sampling Date: Aluminum Chip Drye r August 23 & 24, 2010

General Motors LLC Bedford, IN BT Environmental Consulting,

Inc.

2615 Wolcott Street Ferndale, Michigan N ot to Scale 5 Diameter

6 Diameters

### Bags Samples

to analyzers



## Figure 2

Site: Sampling Date:

USEPA Method 3 A August 23 & 24, 2010

General Motors LLC Bedford, IN Aluminum Chip Drye r BT Environmental Consulting,

Inc.

2615 Wolcott Street Ferndale, Michigan Data Acquisition System



### Calibration Gases (Fed to Probe Tip) Environics Gas Dilution System M&C Model 100-L

O 2 

### Analyzer CAI Series 600

CO 2 

### Analyzer pump tedlar bag

## Figure No. 3

Site: Sampling Date:

USEPA Method 25 A August 23 & 24, 201 0

General Motors LLC Bedford, Indiana BT Environmental Consulting, Inc.

2615 Wolcott Street Ferndale, Michigan Data Acquisition System 

### Heated Sam p le Lin e

Calibration Gases (Fed to Probe Tip) Calibration Line

VIG Total Hydrocarbon AnalyzerFigure No. 4Site: Sampling Date:USEPA Method 0010August 23 & 24, 2010General Motors LLCBedford, IndianaAluminum Chip DryerBT Environmental Consulting, Inc.2615 Wolcott Ferndale,MichiganPumpSilica gelHeated Filter BoxS-Type Pitot w/ ThermocoupleHeated Probe w/ Glass Liner & Glass or SS NozzleMeter RigTemp.ProbeFilterOnOff-+00:001 2 3 4 5Verticle Condenser andSorbent TrapPot Bellied Impinger100 mL DI H2OEmptyFigure No. 5Site: Sampling Date:USEPA Method 0031 August 23 & 24, 2010General Motors LLCBedford, IndianaAluminum Chip DryerBT Environmental Consulting, Inc.2615 Wolcott Ferndale,MichiganPumpSampling ModuleHeated probe with glass linerMeter RigTemp.ProbeFilterOnOff-+00:001 2 3 4 5Charcoal TrapCondensersTenax-GCSorbentTrapsAnasorb-747Sorbent TrapCondensate TrapSilica GelThree Way Glass/TeflonIsolation ValveGlass Wool Filter

# Appendix A Field and Computer Generate d Raw Data and Field NotesCompanyGM BedfordSource DesignationAluminum Chip DryerTest Date8/23/2010Assumed Moisture (Bws)20Test NumberM0031-Run 1Condensate Volume (Vlc)8OperatorTWSilica Gel Weight Gain (Vlc)1Filter NumberNANozzle Diameter (in.)NABarometric Pressure (Pb)30.02Leak Rate Initial0.000@15"Stack Static Pressure (Ps)-0.17Leak Rate Final0.000@14"Stack Dimensions (in.)60Traverse points1Pitot Tube NumberNAPitot Corr. Factor (Cp)NAMeter NumberVOSMeter Corr. Factor (Y)0.98Meter Isokinetic Factor (Kiso)-Orsat Results (%)Delta∆H@0.93CO216.21O22.52Traverse Sampling Time Sampling Stack Temp. Velocity Pres. Orifice Sample VolumeDry Gas Meter Temp. Last ImpingerProbe Filter Box Filter Box ExitPoint (Minutes) Clock Time Train Vac. (F) ("H2O) Differential (cubicfeet) Inlet Outlet Temperature Temperature Temperature TemperatureNumberø (24 hour) ("Hg) Ts∆Ps ("H2O)∆H Vm (F) Tm (F) Tm (F) (F) (F) (F)5 16:58 6 NA NA NA 1240.45 95 95 NA 252 NA NA10 6 NA NA NA 1243.00 96 97 NA 250 NA NA15 6 NA NA NA 1247.50 98 98 NA 250 NA NA20 6 NA NA NA 1250.00 100 100 NA 250 NA NA25 6 NA NA NA 1252.50 101 101 NA 252 NA NA30 6 NA NA NA 1255.00 101 100 NA 251 NA NA35 6 NA NA NA 1257.50 101 101 NA 252 NA NA40 6 NA NA NA 1259.90 101 101 NA 250 NA NA1261.00END - - - - - - - - - - - -5 17:53 3 NA NA NA 1261.00 99 98 NA 249 NA NA10 3 NA NA NA 1264.00 99 98 NA 249 NA NA15 5 NA NA NA 1266.50 99 99 NA 251 NA NA20 5 NA NA NA 1269.00 99 99 NA 248 NA NA25 5 NA NA NA 1271.50 100 101 NA 245 NA NA30 6 NA NA NA 1274.00 102 101 NA 252 NA NA35 6 NA NA NA 1276.50 101 101 NA 251 NA NA40 6 NA NA NA 1279.00 101 100 NA 249 NA NA1281.18END - - - - - - - - - - - -0 18:40 3 NA NA NA 1281.60 98 98 NA 254 NA NA5 4 NA NA NA 1284.00 99 99 NA 249 NA NA10 5 NA NA NA 1286.60 100 99 NA 249 NA NA15 5 NA NA NA 1289.20 100 100 NA 250 NA NA20 6 NA NA NA 1291.60 102 101 NA 249 NA NA25 6 NA NA NA 1294.00 102 101 NA 251 NA NA30 6 NA NA NA 1296.60 102 101 NA 249 NA NA35 6 NA NA NA 1299.00 102 101 NA 252 NA NA401301.43END - - - - - - - - - - - -0 19:30 4 NA NA NA 1302.37 98 98 NA 250 NA NA5 4 NA NA NA 1305.00 100 100 NA 251 NA NA10 5 NA NA NA 1307.60 100 100 NA 250 NA NA15 6 NA NA NA 1310.30 101 100 NA 249 NA NA20 6 NA NA NA 1312.60 100 101 NA 249 NA NA25 6 NA NA NA 1315.10 101 101 NA 251 NA NA30 6 NA NA NA 1317.30 101 101 NA 255 NA NA35 6 NA NA NA 1319.60 101 101 NA 252 NA NA401322.30END - - - - - - - - - - - -Average 40 #DIV/0! #DIV/0! #DIV/0! 77.21 100.0 99.8 #DIV/0! 250.3 #DIV/0! #DIV/0!∆H = Kiso * (Cp)2 * (1-wv/100)2 *(MWm/MWs) * (Ps/Pm) * (Tm/Ts) *∆Ps * D499.88CompanyGM BedfordSource DesignationAluminum Chip DryerTest Date8/24/2010Assumed Moisture (Bws)20Test NumberM0031-Run 2Condensate Volume (Vlc)10OperatorTWSilica Gel Weight Gain (Vlc)0Filter NumberNANozzle Diameter (in.)NABarometric Pressure (Pb)30.08Leak Rate Initial0.000@8"Stack Static Pressure (Ps)-0.17Leak Rate Final0.000@10"Stack Dimensions (in.)60Traverse points1Pitot Tube NumberNAPitot Corr. Factor (Cp)NAMeter NumberVOSMeter Corr. Factor (Y)0.98Meter Isokinetic Factor (Kiso)-Orsat Results (%)Delta∆H@0.93CO216.23O23.09Traverse Sampling Time Sampling Stack Temp. Velocity Pres. Orifice Sample VolumeDry Gas Meter Temp. Last ImpingerProbe Filter Box Filter Box ExitPoint (Minutes) Clock Time Train Vac. (F) ("H2O) Differential (cubicfeet) Inlet Outlet Temperature Temperature Temperature TemperatureNumberø (24 hour) ("Hg) Ts∆Ps ("H2O)∆H Vm (F) Tm (F) Tm (F) (F) (F) (F)5 7:48 4 NA NA NA 1323.10 75 74 NA 255 NA NA10 4 NA NA NA 1325.70 75 74 NA 250 NA NA15 4 NA NA NA 1328.40 75 75 NA 250 NA NA20 5 NA NA NA 1330.80 75 74 NA 249 NA NA25 5 NA NA NA 1333.10 75 74 NA 252 NA NA30 6 NA NA NA 1335.50 76 75 NA 250 NA NA35 6 NA NA NA 1337.90 76 75 NA 250 NA NA40 6 NA NA NA 1340.30 77 75 NA 251 NA NA1342.80END - - - - - - - - - - - -5 8:39 4 NA NA NA 1343.60 76 76 NA 251 NA NA10 4 NA NA NA 1346.10 76 77 NA 251 NA NA15 4 NA NA NA 1348.50 76 77 NA 250 NA NA20 4 NA NA NA 1350.80 76 77 NA 251 NA NA25 4 NA NA NA 1353.20 77 77 NA 250 NA NA30 4 NA NA NA 1355.50 77 78 NA 251 NA NA35 6 NA NA NA 1358.00 77 78 NA 250 NA NA40 6 NA NA NA 1360.50 79 78 NA 255 NA NA1363.75END - - - - - - - - - - - -0 9:28 4 NA NA NA 1364.60 78 78 NA 250 NA NA5 4 NA NA NA 1367.00 78 79 NA 253 NA NA10 5 NA NA NA 1369.60 80 78 NA 249 NA NA15 7 NA NA NA 1371.90 80 79 NA 250 NA NA20 7 NA NA NA 1374.00 81 80 NA 251 NA NA25 6 NA NA NA 1376.60 82 81 NA 250 NA NA30 5 NA NA NA 1379.50 82 81 NA 251 NA NA35 5 NA NA NA 1382.30 83 82 NA 249 NA NA401384.65END - - - - - - - - - - - -0 10:18 5 NA NA NA 1385.55 84 83 NA 251 NA NA5 6 NA NA NA 1388.20 84 85 NA 251 NA NA10 7 NA NA NA 1390.60 86 85 NA 251 NA NA15 7 NA NA NA 1392.90 86 85 NA 248 NA NA20 7 NA NA NA 1395.10 86 86 NA 255 NA NA25 7 NA NA NA 1397.20 86 86 NA 249 NA NA30 7 NA NA NA 1399.60 87 87 NA 251 NA NA35 7 NA NA NA 1402.00 87 87 NA 250 NA NA401404.40END - - - - - - - - - - - -Average 40 #DIV/0! #DIV/0! #DIV/0! 73.00 79.6 79.3 #DIV/0! 250.8 #DIV/0! #DIV/0!∆H = Kiso * (Cp)2 * (1-wv/100)2 *(MWm/MWs) * (Ps/Pm) * (Tm/Ts) *∆Ps * D479.44CompanyGM BedfordSource DesignationAluminum Chip DryerTest Date8/23/2010Assumed Moisture (Bws)20Test NumberM0031-Run 3Condensate Volume (Vlc)9OperatorTWSilica Gel Weight Gain (Vlc)1Filter NumberNANozzle Diameter (in.)NABarometric Pressure (Pb)30.08Leak Rate Initial0.000@15"Stack Static Pressure (Ps)-0.17Leak Rate Final0.000@15"Stack Dimensions (in.)60Traverse points1Pitot Tube NumberNAPitot Corr. Factor (Cp)NAMeter NumberVOSMeter Corr. Factor (Y)0.98Meter Isokinetic Factor (Kiso)-Orsat Results (%)Delta∆H@0.93CO216.57O22.37Traverse Sampling Time Sampling Stack Temp. Velocity Pres. Orifice Sample VolumeDry Gas Meter Temp. Last ImpingerProbe Filter Box Filter Box ExitPoint (Minutes) Clock Time Train Vac. (F) ("H2O) Differential (cubicfeet) Inlet Outlet Temperature Temperature Temperature TemperatureNumberø (24 hour) ("Hg) Ts∆Ps ("H2O)∆H Vm (F) Tm (F) Tm (F) (F) (F) (F)5 11:23 5 NA NA NA 1405.27 87 89 NA 250 NA NA10 5 NA NA NA 1408.60 88 89 NA 249 NA NA15 5 NA NA NA 1411.00 89 90 NA 250 NA NA20 5 NA NA NA 1414.00 90 91 NA 251 NA NA25 5 NA NA NA 1415.80 90 91 NA 250 NA NA30 5 NA NA NA 1418.00 90 92 NA 250 NA NA35 5 NA NA NA 1420.50 90 92 NA 250 NA NA40 6 NA NA NA 1422.60 92 93 NA 253 NA NA1424.80END - - - - - - - - - - - -5 12:12 3 NA NA NA 1425.73 93 94 NA 246 NA NA10 4 NA NA NA 1428.30 93 94 NA 250 NA NA15 5 NA NA NA 1430.60 93 95 NA 250 NA NA20 5 NA NA NA 1433.00 95 96 NA 250 NA NA25 5 NA NA NA 1435.40 95 96 NA 250 NA NA30 5 NA NA NA 1437.60 95 95 NA 252 NA NA35 6 NA NA NA 1440.00 94 93 NA 249 NA NA40 6 NA NA NA 1442.00 93 93 NA 250 NA NA1445.00END - - - - - - - - - - - -0 13:02 4 NA NA NA 1445.92 92 92 NA 249 NA NA5 4 NA NA NA 1449.20 92 92 NA 250 NA NA10 6 NA NA NA 1452.05 92 92 NA 249 NA NA15 6 NA NA NA 1455.40 92 93 NA 249 NA NA20 6 NA NA NA 1458.95 93 94 NA 249 NA NA25 6 NA NA NA 1462.45 94 95 NA 248 NA NA30 6 NA NA NA 1465.15 93 94 NA 251 NA NA35 6 NA NA NA 1467.75 93 93 NA 250 NA NA401470.90END - - - - - - - - - - - -0 13:52 4 NA NA NA 1472.00 93 93 NA 250 NA NA5 5 NA NA NA 1474.25 93 94 NA 250 NA NA10 6 NA NA NA 1476.70 93 93 NA 248 NA NA15 6 NA NA NA 1479.00 92 93 NA 250 NA NA20 6 NA NA NA 1481.50 92 93 NA 248 NA NA25 6 NA NA NA 1484.10 92 93 NA 249 NA NA30 6 NA NA NA 1486.60 92 93 NA 250 NA NA35 6 NA NA NA 1489.10 92 93 NA 252 NA NA401491.50END - - - - - - - - - - - -Average 40 #DIV/0! #DIV/0! #DIV/0! 78.08 92.1 92.9 #DIV/0! 249.8 #DIV/0! #DIV/0!∆H = Kiso * (Cp)2 * (1-wv/100)2 *(MWm/MWs) * (Ps/Pm) * (Tm/Ts) *∆Ps * D492.50BT Environmental Consulting

Isokinetic Run Shee t

Project No.: 10-3997.0 Probe # 6ft B Pollutant Semi-VOS Points/Port 12 Start Finish Pre Post
Company GM DGM # MB-6 Method 0010 Total Points 24 .000 @15"

Location Bedford Rate (cfm) 0.75 Run # 1 Time/pt (min) 8.0 .000 @10" Source AL Chip Dryer Delta ∆ H@ 1.77 Date 8/23/10 Time/reading 4.0 Operator JP Bws (%) 19.9 # of Ports 2 Total Run 192.0
Filter Number 90-Q Condensate Volum e 780 Cp 0.840 Ps (in Hg) 29.97

Barometric 29.98 Silica Gel Weight Gain 52 DGM Y 1.013 Pm (in Hg) 29.98 Ref Temp 68 Static (in H2O) -0.17 Actual Dn (in) 0.48 O2 (%) 16.47 Ref Press 29.92
Stack Dia (ft) 5.00 An (ft^2) 0.00126 CO2 (%) 2.5 Md 29.07 Stack Area (sf) 19.63
Est.DH(in H2O) Ms 26.86 Act. Flow (cfm) 23,417 Must delete extra zeros in the Velocity column

Vmnstd 156.79 Preliminary dP (in H20) Total Vol.(cf) 144.0 Wet Ref Flow (cfm) 16,076

Moisture % 19.99 Preliminary Ts (oF) Est. Us (ft/s) 0.0 Dry Ref Flow (cfm) 12,879
Preliminary Tm (oF) Theor Dn (in) #DIV/0! Comments: " Data Entry Cells "

"Calculated Cells Do Not Touch "

PT # Start Time End Time Clock Time (24hr) DGM Vol. Delta P Stack Temp Meter In Meter Out Desired Delta

H Actual

Delta H Probe Temp. (*F) Filter Temp (*F) Imp temp. (*F) Pump Vac.

1 0.0 4.0 16:49 875.62 0.08 311 89 89 2.26 2.23 255 250 67 6

4.0 8.0 878.96 0.08 310 94 91 2.26 2.24 250 250 66 7.5

2 8.0 12.0 882.33 0.08 308 97 91 2.26 2.26 249 250 64 7.5

12.0 16.0 885.73 0.07 308 99 92 1.98 1.98 250 250 64 7

3 16.0 20.0 888.88 0.07 307 100 92 1.98 1.98 250 250 65 7

20.0 24.0 892.07 0.08 308 101 93 2.26 2.27 249 250 64 7.5

4 24.0 28.0 895.49 0.08 310 103 93 2.26 2.27 250 250 64 7.5

28.0 32.0 898.87 0.08 309 103 94 2.26 2.27 249 250 63 7.5

5 32.0 36.0 902.28 0.07 310 104 94 1.98 1.99 250 250 64 7

36.0 40.0 905.46 0.07 311 104 95 1.98 1.99 249 249 65 7

6 40.0 44.0 908.67 0.09 310 105 95 2.54 2.56 250 250 65 8

44.0 48.0 912.25 0.09 307 105 96 2.54 2.57 251 251 64 8.5

7 48.0 52.0 915.86 0.09 309 106 96 2.54 2.57 250 250 64 8.5

52.0 56.0 919.5 0.09 309 106 97 2.54 2.57 250 250 65 8.5

8 56.0 60.0 923.15 0.09 308 106 97 2.54 2.57 249 248 65 8.5

60.0 64.0 926.78 0.08 310 107 97 2.26 2.28 249 249 64 7.5

9 64.0 68.0 930.21 0.08 310 107 98 2.26 2.57 250 250 65 8

68.0 72.0 933.82 0.09 311 107 98 2.54 2.57 250 250 64 8

10 72.0 76.0 937.45 0.09 310 107 98 2.54 2.57 251 250 64 8

76.0 80.0 941.06 0.09 311 107 98 2.54 2.57 250 249 64 8

11 80.0 84.0 944.67 0.08 310 107 98 2.26 2.28 250 250 64 8

84.0 88.0 948.09 0.08 309 108 99 2.26 2.29 249 250 63 8

12 88.0 92.0 951.55 0.08 309 108 99 2.26 2.29 250 250 63 8

92.0 96.0 954.96 0.08 308 108 99 2.26 2.29 249 249 64 8

1 96.0 100.0 18:2 5 958.39 0.08 306 103 98 2.26 2.29 250 251 66 7.5

100.0 104.0 961.80 0.08 306 104 99 2.26 2.29 249 250 64 7.5

2 104.0 108.0 965.21 0.08 307 106 99 2.26 2.29 249 250 63 8

108.0 112.0 968.64 0.08 306 106 99 2.26 2.3 249 250 63 8

3 112.0 116.0 972.09 0.08 309 107 99 2.26 2.29 250 250 63 8

116.0 120.0 975.52 0.07 310 107 99 1.98 2 250 250 64 7

4 120.0 124.0 978.75 0.08 312 108 99 2.26 2.28 250 251 64 7.5

124.0 128.0 982.15 0.08 313 108 99 2.26 2.28 250 250 63 7.5

5 128.0 132.0 985.58 0.08 313 109 100 2.26 2.28 250 250 63 7.5

132.0 136.0 989.00 0.07 313 109 100 1.98 2 249 249 64 7

6 136.0 140.0 992.21 0.08 312 110 101 2.26 2.29 250 250 64 7.5

140.0 144.0 995.63 0.08 312 110 101 2.26 2.29 251 250 63 7.5

7 144.0 148.0 999.08 0.07 313 110 101 1.98 2 250 250 63 7

148.0 152.0 1002.29 0.07 313 110 102 1.98 2 250 250 62 7

8 152.0 156.0 1005.53 0.07 313 110 102 1.98 2 250 250 62 7

156.0 160.0 1008.76 0.07 313 110 102 1.98 2 251 250 63 7

9 160.0 164.0 1011.97 0.08 313 109 102 2.26 2.29 249 250 64 7.5

164.0 168.0 1015.39 0.08 313 109 102 2.26 2.29 250 249 64 8

10 168.0 172.0 1018.81 0.09 312 109 102 2.54 2.58 250 250 61 8.5

172.0 176.0 1022.45 0.09 314 109 102 2.54 2.57 249 251 59 8.5

11 176.0 180.0 1026.1 0.09 314 109 102 2.54 2.57 250 251 57 8.5

180.0 184.0 1029.76 0.08 312 109 102 2.26 2.29 250 249 57 8.5

12 184.0 188.0 1033.22 0.08 312 108 102 2.26 2.29 251 248 57 8

188.0 192.0 1036.65 0.08 312 108 102 2.26 2.29 250 250 57 8

192.0 20:06 1040.1 - - - - - - - - - - Average: 164.48 0.08 310.3 105.9 98.0 2.27 2.29 249.9 249.9 63.2083333 7.7 Leak CheckBT Environmental Consulting

Isokinetic Run Shee t

Project No.: 10-3997.0 Probe # 6ftB Pollutant Semi-VOS Points/Port 12 Start Finish Pre Post
Company GM DGM # MB-6 Method 10 Total Points 24 0.005 @15"

Location Bedford Rate (cfm) 0.75 Run # 2 Time/pt (min) 8.0 0.005 @13" Source AL Chip Dryer Delta ∆ H@ 1.77 Date 8/24/10 Time/reading 4.0 Operator JP Bws (%) 20.6 # of Ports 2 Total Run 192.0
Filter Number 90-Q Condensate Volum e 833 Cp 0.840 Ps (in Hg) 30.07

Barometric 30.08 Silica Gel Weight Gain 40 DGM Y 1.013 Pm (in Hg) 30.08 Ref Temp 68 Static (in H2O) -0.17 Actual Dn (in) 0.48 O2 (%) 16.29 Ref Press 29.92
Stack Dia (ft) 5.00 An (ft^2) 0.00126 CO2 (%) 3.1 Md 29.15 Stack Area (sf) 19.63
Est.DH(in H2O) Ms 26.85 Act. Flow (cfm) 23,124 Must delete extra zeros in the Velocity column

Vmnstd 157.37 Preliminary dP (in H20) Total Vol.(cf) 144.0 Wet Ref Flow (cfm) 16,168

Moisture % 20.71 Preliminary Ts (oF) Est. Us (ft/s) 0.0 Dry Ref Flow (cfm) 12,836
Preliminary Tm (oF) Theor Dn (in) #DIV/0! Comments: " Data Entry Cells "

"Calculated Cells Do Not Touch "

PT # Start Time End Time Clock Time (24hr) DGM Vol. Delta P Stack Temp Meter In Meter Out Desired Delta

H Actual

Delta H Probe Temp. (*F) Filter Temp (*F) Imp temp. (*F) Pump Vac.

1 0.0 4.0 7:47 40.39 0.08 298 67 67 2.18 2.17 250 253 65 8

4.0 8.0 43.6 0.08 299 70 68 2.18 2.18 250 252 48 9.5

2 8.0 12.0 46.83 0.08 300 71 69 2.18 2.18 250 250 46 9.5

12.0 16.0 50.06 0.08 299 73 69 2.18 2.19 250 250 45 9.5

3 16.0 20.0 53.34 0.07 300 75 69 1.91 1.92 251 250 45 9

20.0 24.0 56.4 0.07 299 76 70 1.91 1.92 250 249 45 8.5

4 24.0 28.0 59.47 0.08 300 78 71 2.18 2.2 250 251 45 9

28.0 32.0 62.72 0.08 299 79 71 2.18 2.2 250 250 46 9.5

5 32.0 36.0 65.95 0.07 300 81 72 1.91 1.93 250 250 47 9

36.0 40.0 69.04 0.07 299 81 72 1.91 1.93 250 249 47 9

6 40.0 44.0 72.13 0.08 300 82 73 2.18 2.21 250 250 47 10

44.0 48.0 75.41 0.08 300 83 73 2.18 2.21 250 250 48 10

7 48.0 52.0 78.7 0.08 300 83 74 2.18 2.22 250 250 48 10

52.0 56.0 82.01 0.09 297 84 74 2.46 2.51 250 248 49 11

8 56.0 60.0 85.5 0.09 298 84 75 2.46 2.5 250 250 47 11

60.0 64.0 89.00 0.09 298 85 75 2.46 2.51 250 249 47 11

9 64.0 68.0 92.51 0.08 299 85 76 2.18 2.23 250 251 47 10

68.0 72.0 95.84 0.08 299 86 76 2.18 2.23 250 251 48 9.5

10 72.0 76.0 95.16 0.08 299 86 77 2.18 2.23 249 249 50 9.5

76.0 80.0 102.45 0.08 299 87 77 2.18 2.23 250 250 50 9.5

11 80.0 84.0 105.76 0.09 297 87 78 2.46 2.52 250 252 51 11

84.0 88.0 109.26 0.09 297 88 78 2.46 2.52 251 251 51 11

12 88.0 92.0 112.79 0.08 296 88 78 2.18 2.25 251 248 52 10

92.0 96.0 9:19 - 9:23 116.12 0.08 296 88 79 2.19 2.25 250 250 52 10

1 96.0 100.0 9:29 119.46 0.08 296 83 79 2.18 2.24 249 249 55 10

100.0 104.0 122.80 0.08 294 86 79 2.18 2.25 250 249 52 10

2 104.0 108.0 126.14 0.08 293 88 80 2.18 2.26 249 250 50 10

108.0 112.0 129.45 0.08 294 89 80 2.18 2.26 251 249 50 10

3 112.0 116.0 132.80 0.08 293 90 81 2.18 2.27 250 250 50 10

116.0 120.0 136.17 0.08 298 91 81 2.18 2.25 250 251 51 10

4 120.0 124.0 139.48 0.09 299 91 81 2.46 2.53 250 250 52 11

124.0 128.0 143 0.09 299 92 82 2.46 2.54 251 251 52 11

5 128.0 132.0 146.53 0.08 300 92 82 2.18 2.25 250 250 53 10.5

132.0 136.0 149.87 0.08 299 92 83 2.18 2.26 250 250 53 10.5

6 136.0 140.0 153.22 0.08 300 93 83 2.18 2.26 250 250 51 10.5

140.0 144.0 156.57 0.08 299 93 84 2.18 2.26 249 251 50 10.5

7 144.0 148.0 159.93 0.08 299 93 84 2.18 2.26 251 251 50 10.5

148.0 152.0 163.28 0.08 299 94 84 2.18 2.26 251 249 52 10.5

8 152.0 156.0 166.65 0.07 300 93 84 1.91 1.98 250 250 50 10.5

156.0 160.0 169.82 0.07 302 94 85 1.91 1.97 250 251 50 10

9 160.0 164.0 172.95 0.07 302 94 85 1.91 1.97 250 249 51 9.5

164.0 168.0 176.12 0.07 301 95 86 1.91 1.98 251 249 50 9.5

10 168.0 172.0 179.28 0.08 301 95 86 2.18 2.26 251 250 53 10

172.0 176.0 182.61 0.08 301 95 86 2.18 2.26 251 250 55 10

11 176.0 180.0 185.96 0.08 301 96 87 2.18 2.27 249 250 52 10

180.0 184.0 189.35 0.08 302 96 87 2.18 2.26 250 250 54 10

12 184.0 188.0 192.71 0.08 303 96 87 2.18 2.26 250 250 56 10

188.0 192.0 196.09 0.07 303 96 87 1.91 1.98 251 250 54 10

192.0 11:0 5 199.25 Average: 158.86 0.08 298.9 86.8 78.4 2.17 2.22 250.1 250.0 50.3 10 Leak CheckBT Environmental Consulting

Isokinetic Run Shee t

Project No.: 10-3997.0 Probe # 6ft B Pollutant S emi-Volatil e Points/Port 12 Start Finish Pre Post
Company GM DGM # MB-6 Method 0010 Total Points 24 .01 @15"

Location Bedford Rate (cfm) Run # 3 Time/pt (min) 8.0 .01 @13" Source AL Chip Dryer Delta ∆ H@ 1.77 Date 8/24/10 Time/reading 4.0 Operator JP Bws (%) 18.87 # of Ports 2 Total Run 192.0
Filter Number 90-Q Condensate Volum e 735 Cp 0.840 Ps (in Hg) 30.07

Barometric 30.08 Silica Gel Weight Gain 38 DGM Y 1.013 Pm (in Hg) 30.08 Ref Temp 68 Static (in H2O) -0.17 Actual Dn (in) 0.48 O2 (%) 16 Ref Press 29.92
Stack Dia (ft) 5.00 An (ft^2) 0.00126 CO2 (%) 3.0 Md 29.12 Stack Area (sf) 19.63
Est.DH(in H2O) Ms 27.02 Act. Flow (cfm) 22,831 Must delete extra zeros in the Velocity column

Vmnstd 155.55 Preliminary dP (in H20) Total Vol.(cf) 0.0 Wet Ref Flow (cfm) 15,887

Moisture % 18.96 Preliminary Ts (oF) Est. Us (ft/s) 0.0 Dry Ref Flow (cfm) 12,889
Preliminary Tm (oF) Theor Dn (in) #DIV/0! Comments: " Data Entry Cells "

"Calculated Cells Do Not Touch "

PT # Start Time End Time Clock Time (24hr) DGM Vol. Delta P Stack Temp Meter In Meter Out Desired Delta

H Actual

Delta H Probe Temp. (*F) Filter Temp (*F) Imp temp. (*F) Pump Vac.

1 0.0 4.0 11:52 200.26 0.07 302 85 85 2.01 1.96 251 252 65 8.5

4.0 8.0 203.35 0.07 303 88 85 2.01 1.96 253 252 65 9.5

2 8.0 12.0 206.47 0.08 304 90 85 2.30 2.24 251 252 60 10

12.0 16.0 209.83 0.08 304 92 85 2.30 2.25 249 251 54 10

3 16.0 20.0 213.14 0.08 306 93 86 2.30 2.24 250 250 52 10

20.0 24.0 216.48 0.08 302 94 86 2.30 2.26 249 250 52 10

4 24.0 28.0 219.96 0.08 302 96 87 2.30 2.26 251 250 51 10

28.0 32.0 223.24 0.07 300 96 87 2.01 1.99 251 251 52 9.5

5 32.0 36.0 226.44 0.07 304 96 87 2.01 1.98 248 250 51 9.5

36.0 40.0 229.61 0.07 303 96 88 2.01 1.98 248 250 51 9.5

6 40.0 44.0 232.78 0.08 301 96 88 2.30 2.27 219 250 52 10

44.0 48.0 236.15 0.07 301 96 89 2.01 1.99 250 250 52 9.5

7 48.0 52.0 239.32 0.07 301 99 89 2.01 1.99 250 250 52 9.5

52.0 56.0 242.49 0.08 299 96 89 2.30 2.28 250 248 52 10

8 56.0 60.0 245.84 0.08 300 96 89 2.30 2.56 251 252 52 11

60.0 64.0 249.44 0.09 301 96 89 2.59 2.55 250 251 52 11

9 64.0 68.0 253.01 0.08 301 97 89 2.30 2.27 251 250 52 10

68.0 72.0 256.42 0.08 301 97 89 2.30 2.27 249 253 53 10

10 72.0 76.0 259.77 0.08 302 97 89 2.30 2.27 250 248 53 10

76.0 80.0 263.14 0.08 303 97 89 2.30 2.27 249 249 52 10

11 80.0 84.0 266.51 0.08 304 97 90 2.30 2.27 251 247 52 10

84.0 88.0 269.91 0.09 304 97 90 2.59 2.55 249 251 53 11

12 88.0 92.0 273.5 0.08 305 98 90 2.30 2.27 250 250 52 10

92.0 96.0 13:24 - 13:2 8 276.87 0.08 305 98 90 2.30 2.27 250 250 53 10

1 96.0 100.0 13:32 280.27 0.08 302 83 90 2.30 2.26 250 250 56 10

100.0 104.0 283.62 0.08 300 97 91 2.30 2.28 249 249 53 10

2 104.0 108.0 287 0.09 300 98 91 2.59 2.57 250 248 52 11

108.0 112.0 290.57 0.09 300 99 91 2.59 2.57 251 253 52 11

3 112.0 116.0 294.19 0.08 302 99 91 2.30 2.28 250 250 54 10

116.0 120.0 297.59 0.08 303 99 91 2.30 2.28 250 248 57 10

4 120.0 124.0 300.99 0.08 304 99 91 2.30 2.27 250 250 57 10

124.0 128.0 304.35 0.08 304 100 92 2.30 2.28 249 247 56 10

5 128.0 132.0 307.74 0.08 302 100 92 2.30 2.28 250 250 57 10

132.0 136.0 311.15 0.08 301 100 92 2.30 2.29 250 253 57 10

6 136.0 140.0 314.56 0.08 302 100 92 2.30 2.28 249 250 54 10

140.0 144.0 317.97 0.07 302 100 92 2.01 2.28 249 251 53 10

7 144.0 148.0 321.36 0.07 302 99 92 2.01 2 251 249 53 9.5

148.0 152.0 324.35 0.07 303 99 92 2.01 1.99 250 250 55 9.5

8 152.0 156.0 327.74 0.07 304 100 92 2.01 1.99 250 250 55 9.5

156.0 160.0 330.91 0.08 306 100 92 2.30 1.99 249 250 56 9.5

9 160.0 164.0 334.1 0.08 305 101 93 2.30 2.28 253 249 57 10

164.0 168.0 337.5 0.08 303 101 93 2.30 2.28 252 250 56 10

10 168.0 172.0 340.88 0.08 303 101 93 2.30 2.28 251 252 57 10

172.0 176.0 344.29 0.08 302 100 93 2.30 2.28 249 250 55 10

11 176.0 180.0 347.7 0.07 303 99 93 2.01 1.99 251 251 57 9.5

180.0 184.0 350.89 0.07 304 99 93 2.01 1.99 250 250 59 9.5

12 184.0 188.0 354.08 0.07 304 98 93 2.01 1.99 250 251 60 9.5

188.0 192.0 357.24 0.07 303 98 93 2.01 1.99 251 250 62 9.5

192.0 15:08 360.42 Average: 160.16 0.08 302.5 96.9 90.0 2.23 2.21 249 250 54.6875 10 Leak Check

# Appendix B

Calibration Data

### ANALYZER CALIBRATION ERROR CHECK DATA

Test Date: 8/23/2010 Analyzer: Teledyne 300E 

### Client: GM Bedford Serial #: 288


### Unit: Chip Dryer Span: 22.40 Sample Location: Exhaust Recorder Range: -5 to 95% FS Calibration Gas: O2 Concentration: 22.4, 10.0 Cylinder #: Units: % Zero Gas: Nitrogen

Cylinder Analyzer Absolute Difference Value Response Difference (% of Span) ppm ppm ppm *

Zero Gas 0.00 0.00 0.00 0.00

Mid Gas 10.00 10.18 0.18 0.80 High Gas 22.40 22.37 0.03 0.13

* Eq. 7E-1 (Cdir - Cv)

ACE = CS x 100

Where: ACE = Analyzer calibratoin error, % of span Cdir = Measured concentration of a cal gas when introduced in direct cal mode

Cv = Manufacturer cirtified concentration of cal gas CS = Calibration Span

ANALYZER CALIBRATION ERROR CHECK DATA

Test Date: 8/23/2010 Analyzer: Teledyne Infrared 

### Client: GM Bedford Serial #: Unit: Chip Dryer Span: 18.10 Sample Location: Exhaust Recorder Range: -5 to 95% FS Calibration Gas: CO2 Concentration: 10.08, 18.1 Cylinder #: CC28908 Units: % Zero Gas: Nitrogen

Cylinder Analyzer Absolute Difference Value Response Difference (% of Span) ppm ppm ppm *

Zero Gas 0.00 0.00 0.00 0.00

Mid Gas 10.08 10.17 0.09 0.50 High Gas 18.10 17.98 0.12 0.66

* Eq. 7E-1 (Cdir - Cv)

ACE = CS x 100

Where: ACE = Analyzer calibratoin error, % of span Cdir = Measured concentration of a cal gas when introduced in direct cal mode

Cv = Manufacturer cirtified concentration of cal gas CS = Calibration Span

### CEMS DRIFT CALCULATION SPREAD SHEET

Client: GM Bedford

Source: Chip Dryer

Date: 8/23/2010 Span: 22.40 18.10 22.4 18.1

O2 CO2 O2 CO2

Calibration Gas Value = 10.00 10.08 10 10.08

Run #1 Initial Zero Bias Value = 0 0.01 analyzer 0.00 0.00 Run #1 Initial System Bias Value = 10.18 10.17 system 0.14 0.01 Run #1 Average = 16.47 2.54 RUN 1 Run #1 Final Zero Bias Value = 0.14 0.01 analyzer 10.18 10.17 Run #1 Final System Bias Value = 10.19 10.12 system 10.19 10.12

Run #1 Total Drift Corrected = 16.21 2.52 F Factor = 8710

zero calibration drift = 3% 0.63 0.00 zero bias 0.63 0.06 5% allowe d calibration drift = 0.04 -0.28 span bias 0.04 -0.28

Drift Correction calculation

Where: Cgas =effluent gas concentration, dry basis, ppm C = avg. gas concentration indicated by analyzer, dry basis, ppm Co = avg. of initial and final system calibration bias check for the zero gas Cm = avg. of initial and final system calibration bias check for the upscale calibration gas Cma = actual concentration of the upscale calibration gas, ppm o m ma

o gas 

# C C C C C C

− − = ) (

### ANALYZER CALIBRATION ERROR CHECK DATA

Test Date: 8/24/2010 Analyzer: Teledyne 300E


### Client: GM Bedford Serial #: 288


### Unit: Chip Dryer Span: 22.40 Sample Location: Exhaust Recorder Range: -5 to 95% FS Calibration Gas: O2 Concentration: 22.4, 10.0 Cylinder #: EB0013835 Units: % Zero Gas: Nitrogen

Cylinder Analyzer Absolute Difference Value Response Difference (% of Span) ppm ppm ppm *

Zero Gas 0.00 0.18 0.18 0.80

Mid Gas 10.00 10.10 0.10 0.45 High Gas 22.40 22.40 0.00 0.00

* Eq. 7E-1 (Cdir - Cv)

ACE = CS x 100

Where: ACE = Analyzer calibratoin error, % of span Cdir = Measured concentration of a cal gas when introduced in direct cal mode

Cv = Manufacturer cirtified concentration of cal gas CS = Calibration Span

ANALYZER CALIBRATION ERROR CHECK DATA

Test Date: 8/24/2010 Analyzer: Teledyne Infrared


### Client: GM Bedford Serial #: Unit: Chip Dryer Span: 18.10 Sample Location: Exhaust Recorder Range: -5 to 95% FS Calibration Gas: CO2 Concentration: 10.08, 18.1 Cylinder #: CC28908 Units: % Zero Gas: Nitrogen

Cylinder Analyzer Absolute Difference Value Response Difference (% of Span) ppm ppm ppm *

Zero Gas 0.00 0.00 0.00 0.00

Mid Gas 10.08 10.10 0.02 0.11 High Gas 18.10 18.01 0.09 0.50

### CEMS DRIFT CALCULATION SPREAD SHEET

Client: GM Bedford

Source: Chip Dryer

Date: 8/24/2010 Span: 22.40 18.10 22.4 18.1

O2 CO2 O2 CO2

Calibration Gas Value = 10.00 10.08 10 10.08

Run #1 Initial Zero Bias Value = 0.18 0 analyzer 0.18 0.00 Run #1 Initial System Bias Value = 10.1 10.1 system 0.12 0.01 Run #1 Average = 16.29 3.10 RUN 2 Run #1 Final Zero Bias Value = 0.12 0.01 analyzer 10.10 10.10 Run #1 Final System Bias Value = 10.09 10.12 system 10.09 10.12

Run #1 Total Drift Corrected = 16.23 3.09 F Factor = 8710

zero calibration drift = 3% -0.27 0.06 zero bias -0.27 0.06 5% allowe d calibration drift = -0.04 0.11 span bias -0.04 0.11

Run #2 Initial Zero Bias Value = 0.12 0.01 analyzer 0.18 0 Run #2 Initial System Bias Value = 10.09 10.12 system 0.10 0.01 Run #2 Average = 16.66 2.37 RUN 3 Run #2 Final Zero Bias Value = 0.1 0.01 analyzer 10.1 10.1 Run #2 Final System Bias Value = 10.11 10.01 system 10.11 10.01

Run #2 Total Drift Corrected = 16.57 2.37 F Factor = 8710

zero calibration drift = -0.09 0.00 zero bias -0.36 0.06 calibration drift = 0.09 -0.61 span bias 0.04 -0.50

Drift Correction calculation

Where: Cgas =effluent gas concentration, dry basis, ppm C = avg. gas concentration indicated by analyzer, dry basis, ppm Co = avg. of initial and final system calibration bias check for the zero gas Cm = avg. of initial and final system calibration bias check for the upscale calibration gas Cma = actual concentration of the upscale calibration gas, ppm o m ma

o gas 

# C C C C C C

− − = ) (Plant:GM BedfordOutlet Calibration response, ppmC3H8 AnalyzerLocation:Aluminum Chip DryerCalibration System injection cal. error,Date: gas conc., Pretest PostT 1 PostT 2 PostT 3 % ofDrift, % of spanppmC3H814:10:00 20:42:00cal. gas Test 1 Test 2 Test 3Test no.:Run 10.000.120.11-0.029.919.839.88-0.81 0.10Operator:JS31.1631.09 -0.2249.9949.87 -0.24Monitor:Outlet: VIG THC: PASSSpan value,49.99 Outlet* AS DEFINED BY EPA METHOD 25A, THESE THREE VALUES MUST BE THE SAME.Analyzer cal. error, % of cal. gas = (sys. pretest cal. response, ppmC3H8 - cal. gas conc., ppmC3H8)X100%/(cal. gas conc., ppmC3H8): Limit = 5%.Drift, % of span = (relevant posttest sys. inj. cal. response,ppmC3H8 - sys. pretest cal. response, ppmC3H8)X100%/(span value,ppmC3H8): Limit = 3%.System response time (95% of response for high cal. gas), sec. = 1st: 15 2nd: 15 3rd: 15 Average: 15 Limit =30secAugust 23, 2010Plant:GM BedfordOutlet Calibration response, ppmC3H8 AnalyzerLocation:Aluminum Chip DryerCalibration System injection cal. error,Date: gas conc., Pretest PostT 2 PostT 3 % ofDrift, % of spanppmC3H87:30:00 11:23:00 15:10:00cal. gas Test 2 Test 3Test no.:Runs 2 & 30.000.17-0.03 0.18-0.40 0.029.9110.109.86 9.891.92 -0.48 -0.42Operator:JS31.1631.33 0.5549.9949.92 -0.14Monitor:Outlet: JUM 109A THC: PASSSpan value,49.99 Outlet* AS DEFINED BY EPA METHOD 25A, THESE THREE VALUES MUST BE THE SAME.Analyzer cal. error, % of cal. gas = (sys. pretest cal. response, ppmC3H8 - cal. gas conc., ppmC3H8)X100%/(cal. gas conc., ppmC3H8): Limit = 5%.Drift, % of span = (relevant posttest sys. inj. cal. response,ppmC3H8 - sys. pretest cal. response, ppmC3H8)X100%/(span value,ppmC3H8): Limit = 3%.System response time (95% of response for high cal. gas), sec. = 1st: 152nd: 15 3rd: 15 Average: 15 Limit =30secAugust 24th, 2010

# Appendix C

RAW CEM Data

# Appendix D Laboratory Analytical Results

### Your Project #: 10-3997.00
Site: GM-BEDFORD

Your C.O.C. #: N/A

Attention: James K. Sharp

BT Environmental Consulting

2615 Wolcott St. Ferndale, MI
USA 48220

Report Date: 2010/09/23

This report supersedes all previous reports with the same Maxxam job number



## CERTIFICATE

OF ANALYSIS

MAXXAM JOB #: B0B9532

Received: 2010/08/31, 12:00

Sample Matrix: AIR

# Samples Received: 14

Date Date Method Analyses Quantity Extracted Analyzed Laboratory Method Reference

VOST Analysis (5041mod) 5 N/A 2010/09/01 BRL SOP-00302 EPA 5041mod(M0030)

VOST Analysis (5041mod) 9 N/A 2010/09/02 BRL SOP-00302 EPA 5041mod(M0030)



### Sample Matrix: Water

# Samples Received: 4

Date Date Method Analyses Quantity Extracted Analyzed Laboratory Method Reference

Volatile Open Characterization ( 1 ) 4 N/A 2010/09/03 CAM SOP-00226 EPA 8260
VOST Condensate (8260Cmod) 4 N/A 2010/09/03 BRL SOP-00305 EPA 8260Cmod(M0030)

* RPDs calculated using raw data. The rounding of final results may result in the apparent difference.

(1) Sample(s) analyzed using methodologies that have not been subjected to Maxxam's standard validation process for the submitted matrix

and is not an Accredited method. Analysis performed with client consent, however results should be viewed with discretion.



### Encryption

Key

Please direct all questions regarding this Certificate of Analysis to your Project Manager.

LINA BARRETO, Project Manager

Email: Lina.Barreto@maxxamanalytics.com

Phone# (905) 817-5700

==================================================================== Maxxam has procedures in place to guard against improper use of the electronic signature and have the required "signatories", as per section

5.10.2 of ISO/IEC 17025:2005(E), signing the reports. For Service Group specific validation please refer to the Validation Signature Page.

Total cover pages: 1

Page 1 of 12

### BT Environmental Consulting

Maxxam Job #: B0B9532 Client Project #: 10-3997.00 Report Date: 2010/09/23 Project name: GM-BEDFORD



### VOLATILE ORGANICS BY GC/MS (AIR)

Maxxam ID G Z 7 5 3 9 G

Z 7 5 4 0 G

Z 7 5 4 1 G

Z 7 5 4 2 G

Z 7 5 4 3 Sampling Date 2010/08/23 2010/08/23 2010/08/23

COC Number N/A N/A N/A N/A N/A

U n i t s TRIP TRAIN RUN 1-SET RUN 1-SET RUN 1-SET RDL QC Batch

BLK-M0031-#4 BLK-M0031-#15 1-M0031-#6 2-M0031-#14 3-M0031-#5

Trichlorofluoromethane (FREON 11) ug ND ND 0.02 0.02 0.02 0.01 2253781

1,1-Dichloroethylene ug ND ND ND ND ND 0.01 2253781

Carbon Disulfide ug ND ND ND ND ND 0.03 2253781

Methylene Chloride(Dichloromethane) ug ND ND 4.63 0.69 0.77 0.02 2253781

1,1-Dichloroethane ug ND ND ND ND ND 0.01 2253781

trans-1,2-Dichloroethylene ug ND ND ND ND ND 0.01 2253781

Chloroform ug ND ND 0.21 0.28 0.20 0.01 2253781

1,2-Dichloroethane ug ND ND ND ND ND 0.007 2253781

1,1,1-Trichloroethane ug ND ND ND ND ND 0.01 2253781

Carbon Tetrachloride ug ND ND ND ND ND 0.02 2253781

Benzene ug ND ND 2.67 2.35 0.378 0.009 2253781

1,1,2-Trichloroethane ug ND ND ND ND ND 0.02 2253781

1,2-Dichloropropane ug ND ND ND ND ND 0.01 2253781

Trichloroethylene ug ND ND 0.02 0.02 0.01 0.01 2253781

Dibromomethane ug ND ND ND ND ND 0.01 2253781

Bromodichloromethane ug ND ND 0.06 0.06 0.05 0.01 2253781

cis-1,3-Dichloropropene ug ND ND ND ND ND 0.01 2253781

trans-1,3-Dichloropropene ug ND ND ND ND ND 0.007 2253781

Dibromochloromethane ug ND ND 0.021 0.022 0.021 0.009 2253781

Toluene ug ND ND 0.13 0.07 0.03 0.01 2253781

Tetrachloroethylene ug ND ND ND 0.02 ND 0.02 2253781

Acrylonitrile ug ND ND 0.34 0.33 0.10 0.03 2253781

Chloroprene ug ND ND ND ND ND 0.03 2253781

Surrogate Recovery (%)

Bromofluorobenzene % 99 98 96 96 96 2253781

D10-Ethylbenzene (FS) % 120 118 111 116 116 2253781

D4-1,2-Dichloroethane % 112 112 108 107 109 2253781

D8-Toluene % 100 97 94 96 94 2253781

ND = Not detected

N/A = Not Applicable

RDL = Reportable Detection Limit
QC Batch = Quality Control Batch

Page 2 of 12

### BT Environmental Consulting

Maxxam Job #: B0B9532 Client Project #: 10-3997.00 Report Date: 2010/09/23 Project name: GM-BEDFORD



### VOLATILE ORGANICS BY GC/MS (AIR)

Maxxam ID G Z 7 5 4 4 G

Z 7 5 4 5 G

Z 7 5 4 6 G

Z 7 5 4 8 G

Z 7 5 4 9 Sampling Date 2010/08/23 2010/08/24 2010/08/24 2010/08/24 2010/08/24

COC Number N/A N/A N/A N/A N/A

U n i t s RUN 1-SET RUN 2-SET RUN 2-SET RUN 2-SET RUN 2-SET RDL QC Batch

4-M0031-#12 1-M0031-#2 2-M0031-#1 3-M0031-#9 4-M0031-#10

Trichlorofluoromethane (FREON 11) ug 0.02 0.02 0.03 0.02 0.04 0.01 2254579

1,1-Dichloroethylene ug ND ND ND ND ND 0.01 2254579

Carbon Disulfide ug ND ND ND ND ND 0.03 2254579

Methylene Chloride(Dichloromethane) ug 1.48 1.91 0.37 0.32 0.45 0.02 2254579

1,1-Dichloroethane ug ND ND ND ND ND 0.01 2254579

trans-1,2-Dichloroethylene ug ND ND ND ND ND 0.01 2254579

Chloroform ug 0.18 0.17 0.17 0.19 0.17 0.01 2254579

1,2-Dichloroethane ug ND ND ND ND ND 0.007 2254579

1,1,1-Trichloroethane ug ND ND ND ND ND 0.01 2254579

Carbon Tetrachloride ug ND ND ND ND ND 0.02 2254579

Benzene ug 0.757 0.250 0.538 0.878 0.671 0.009 2254579

1,1,2-Trichloroethane ug ND ND ND ND ND 0.02 2254579

1,2-Dichloropropane ug ND ND ND ND ND 0.01 2254579

Trichloroethylene ug ND ND ND ND ND 0.01 2254579

Dibromomethane ug ND ND ND ND ND 0.01 2254579

Bromodichloromethane ug 0.05 0.05 0.06 0.06 0.05 0.01 2254579

cis-1,3-Dichloropropene ug ND ND ND ND ND 0.01 2254579

trans-1,3-Dichloropropene ug ND ND ND ND ND 0.007 2254579

Dibromochloromethane ug 0.016 0.023 0.024 0.024 0.021 0.009 2254579

Toluene ug 0.03 0.03 0.03 0.03 0.03 0.01 2254579

Tetrachloroethylene ug ND ND ND ND ND 0.02 2254579

Acrylonitrile ug 0.14 0.08 0.13 0.19 0.15 0.03 2254579

Chloroprene ug ND ND ND ND ND 0.03 2254579

Surrogate Recovery (%)

Bromofluorobenzene % 94 98 99 97 99 2254579

D10-Ethylbenzene (FS) % 125 109 115 111 110 2254579

D4-1,2-Dichloroethane % 112 109 108 108 110 2254579

D8-Toluene % 96 96 94 93 95 2254579

ND = Not detected

N/A = Not Applicable

RDL = Reportable Detection Limit
QC Batch = Quality Control Batch

Page 3 of 12

### BT Environmental Consulting

Maxxam Job #: B0B9532 Client Project #: 10-3997.00 Report Date: 2010/09/23 Project name: GM-BEDFORD



### VOLATILE ORGANICS BY GC/MS (AIR)

Maxxam ID G Z 7 5 5 0 G

Z 7 5 5 1 G

Z 7 5 5 2 G

Z 7 5 5 3 Sampling Date 2010/08/24 2010/08/24 2010/08/24 2010/08/24

COC Number N/A N/A N/A N/A

U n i t s RUN 3-SET RUN 3-SET RUN 3-SET RUN 3-SET RDL QC Batch

1-M0031-#3 2-M0031-#13 3-M0031-#8 4-M0031-#11

Trichlorofluoromethane (FREON 11) ug 0.03 0.02 0.02 0.01 0.01 2254579

1,1-Dichloroethylene ug ND ND ND ND 0.01 2254579

Carbon Disulfide ug ND ND ND ND 0.03 2254579

Methylene Chloride(Dichloromethane) ug 0.54 0.39 0.16 0.30 0.02 2254579

1,1-Dichloroethane ug ND ND ND ND 0.01 2254579

trans-1,2-Dichloroethylene ug ND ND ND ND 0.01 2254579

Chloroform ug 0.15 0.17 0.15 0.15 0.01 2254579

1,2-Dichloroethane ug ND ND ND ND 0.007 2254579

1,1,1-Trichloroethane ug ND ND ND ND 0.01 2254579

Carbon Tetrachloride ug ND ND ND ND 0.02 2254579

Benzene ug 0.821 1.45 0.427 0.750 0.009 2254579

1,1,2-Trichloroethane ug ND ND ND ND 0.02 2254579

1,2-Dichloropropane ug ND ND ND ND 0.01 2254579

Trichloroethylene ug ND ND ND ND 0.01 2254579

Dibromomethane ug ND ND ND ND 0.01 2254579

Bromodichloromethane ug 0.04 0.05 0.05 0.04 0.01 2254579

cis-1,3-Dichloropropene ug ND ND ND ND 0.01 2254579

trans-1,3-Dichloropropene ug ND ND ND ND 0.007 2254579

Dibromochloromethane ug 0.017 0.018 0.018 0.017 0.009 2254579

Toluene ug 0.06 0.12 0.02 0.03 0.01 2254579

Tetrachloroethylene ug ND ND ND ND 0.02 2254579

Acrylonitrile ug 0.16 0.22 0.09 0.11 0.03 2254579

Chloroprene ug ND ND ND ND 0.03 2254579

Surrogate Recovery (%)

Bromofluorobenzene % 97 96 96 96 2254579

D10-Ethylbenzene (FS) % 118 113 109 112 2254579

D4-1,2-Dichloroethane % 109 111 109 110 2254579

D8-Toluene % 96 95 95 97 2254579

ND = Not detected

N/A = Not Applicable

RDL = Reportable Detection Limit
QC Batch = Quality Control Batch

Page 4 of 12

### BT Environmental Consulting

Maxxam Job #: B0B9532 Client Project #: 10-3997.00 Report Date: 2010/09/23 Project name: GM-BEDFORD



### VOLATILE ORGANICS BY GC/MS (WATER)

Maxxam ID G Z 7 5 5 4 G

Z 7 5 5 5 G

Z 7 5 5 6 G

Z 7 5 5 7 Sampling Date 2010/08/23 2010/08/24 2010/08/24

COC Number N/A N/A N/A N/A

U n i t s BLANK-M0031-COND RDL RUN RUN RUN RDL QC Batch

1-M0031-COND 2-M0031-COND 3-M0031-COND

Miscellaneous Organics ug/L 0.0 N/A 0.0 0.0 0.0 N/A 2267562

Trichlorofluoromethane (FREON 11) ug/L ND 4.0 ND ND ND 40 2252937

1,1-Dichloroethylene ug/L ND 2.0 ND ND ND 20 2252937

Carbon Disulfide ug/L ND 1.0 ND ND ND 10 2252937

Methylene Chloride(Dichloromethane) ug/L 9.7 2.0 2000 1900 1700 20 2252937

1,1-Dichloroethane ug/L ND 0.80 ND ND ND 8.0 2252937

trans-1,2-Dichloroethylene ug/L ND 2.0 ND ND ND 20 2252937

Chloroform ug/L 1.8 0.80 ND ND ND 8.0 2252937

1,2-Dichloroethane ug/L ND 1.0 ND ND ND 10 2252937

1,1,1-Trichloroethane ug/L ND 1.0 ND ND ND 10 2252937

Carbon Tetrachloride ug/L ND 1.0 ND ND ND 10 2252937

Benzene ug/L ND 1.0 ND ND ND 10 2252937

1,1,2-Trichloroethane ug/L ND 1.0 ND ND ND 10 2252937

1,2-Dichloropropane ug/L ND 1.0 ND ND ND 10 2252937

Trichloroethylene ug/L ND 1.0 ND ND ND 10 2252937

Dibromomethane ug/L ND 1.0 ND ND ND 10 2252937

Bromodichloromethane ug/L ND 0.80 ND ND ND 8.0 2252937

cis-1,3-Dichloropropene ug/L ND 0.80 ND ND ND 8.0 2252937

trans-1,3-Dichloropropene ug/L ND 1.2 ND ND ND 12 2252937

Dibromochloromethane ug/L ND 0.80 ND ND ND 8.0 2252937

Toluene ug/L ND 1.0 21 34 33 10 2252937

Tetrachloroethylene ug/L ND 1.0 ND ND ND 10 2252937

Acrylonitrile ug/L ND 10 ND ND ND 100 2252937

Surrogate Recovery (%)

4-Bromofluorobenzene % 91 91 91 91 2252937

D4-1,2-Dichloroethane % 110 119 114 121 2252937

D8-Toluene % 103 100 104 103 2252937

ND = Not detected

N/A = Not Applicable

RDL = Reportable Detection Limit
QC Batch = Quality Control Batch

Page 5 of 12

### BT Environmental Consulting

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### Test Summary

Maxxam ID GZ7539 Collected Sample ID TRIP BLK-M0031-#4 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2253781 N/A 2010/09/01 YYA

Maxxam ID GZ7540 Collected Sample ID TRAIN BLK-M0031-#15 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2253781 N/A 2010/09/01 YYA

Maxxam ID GZ7541 Collected 2010/08/23 Sample ID RUN 1-SET 1-M0031-#6 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2253781 N/A 2010/09/01 YYA

Maxxam ID GZ7542 Collected 2010/08/23 Sample ID RUN 1-SET 2-M0031-#14 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2253781 N/A 2010/09/01 YYA

Maxxam ID GZ7543 Collected 2010/08/23 Sample ID RUN 1-SET 3-M0031-#5 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2253781 N/A 2010/09/01 YYA

Maxxam ID GZ7544 Collected 2010/08/23 Sample ID RUN 1-SET 4-M0031-#12 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Maxxam ID GZ7545 Collected 2010/08/24 Sample ID RUN 2-SET 1-M0031-#2 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Page 6 of 12

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### Test Summary

Maxxam ID GZ7546 Collected 2010/08/24 Sample ID RUN 2-SET 2-M0031-#1 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Maxxam ID GZ7548 Collected 2010/08/24 Sample ID RUN 2-SET 3-M0031-#9 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Maxxam ID GZ7549 Collected 2010/08/24 Sample ID RUN 2-SET 4-M0031-#10 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Maxxam ID GZ7550 Collected 2010/08/24 Sample ID RUN 3-SET 1-M0031-#3 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Maxxam ID GZ7551 Collected 2010/08/24 Sample ID RUN 3-SET 2-M0031-#13 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Maxxam ID GZ7552 Collected 2010/08/24 Sample ID RUN 3-SET 3-M0031-#8 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Maxxam ID GZ7553 Collected 2010/08/24 Sample ID RUN 3-SET 4-M0031-#11 Shipped

Matrix AIR Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

VOST Analysis (5041mod) GC /MS 2254579 N/A 2010/09/02 YYA

Page 7 of 12

### BT Environmental Consulting

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### Test Summary

Maxxam ID GZ7554 Collected Sample ID BLANK-M0031-COND Shipped

Matrix Water Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

Volatile Open Characterization P&T /MS 2267562 N/A 2010/09/03 AH

VOST Condensate (8260Cmod) P&T /MS 2252937 N/A 2010/09/03 AGE

Maxxam ID GZ7555 Collected 2010/08/23 Sample ID RUN 1-M0031-COND Shipped

Matrix Water Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

Volatile Open Characterization P&T /MS 2267562 N/A 2010/09/03 AH

VOST Condensate (8260Cmod) P&T /MS 2252937 N/A 2010/09/03 AGE

Maxxam ID GZ7556 Collected 2010/08/24 Sample ID RUN 2-M0031-COND Shipped

Matrix Water Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

Volatile Open Characterization P&T /MS 2267562 N/A 2010/09/03 AH

VOST Condensate (8260Cmod) P&T /MS 2252937 N/A 2010/09/03 AGE

Maxxam ID GZ7557 Collected 2010/08/24 Sample ID RUN 3-M0031-COND Shipped

Matrix Water Received 2010/08/31

Test Description Instrumentation Batch Extracted Analyzed Analyst

Volatile Open Characterization P&T /MS 2267562 N/A 2010/09/03 AH

VOST Condensate (8260Cmod) P&T /MS 2252937 N/A 2010/09/03 AGE

Page 8 of 12

### BT Environmental Consulting

Maxxam Job #: B0B9532 Client Project #: 10-3997.00 Report Date: 2010/09/23 Project name: GM-BEDFORD

GENERAL COMMENTS

VOC Analysis: Due to high concentrations of target analytes, most of the samples required dilution. Detection limits were adjusted accordingly.

VOC Analysis: The results for the open characterization are provided as a separate attachment.

Sample GZ7541-01: Dichloromethane and benzene are over the calibration range. Data should be considered an estimate only.

Sample GZ7542-01: Benzene is over the calibration range. Data should be considered an estimate only.

Sample GZ7544-01: Dichloromethane is over the calibration range. Data should be considered an estimate only.

Sample GZ7545-01: Dichloromethane is over the calibration range. Data should be considered an estimate only.

Sample GZ7551-01: Benzene is over the calibration range. Data should be considered an estimate only.

Sample GZ7554-01: VOC Analysis: Due to insufficient sample volume, sample required dilution. Detection limits were adjusted accordingly.

VOC Analysis: Sample volume received = 43mL.

Sample GZ7555-01: VOC Analysis: Sample volume received = 43mL.

Sample GZ7556-01: VOC Analysis: Sample volume received = 43mL.

Sample GZ7557-01: VOC Analysis: Sample volume received = 43mL.

Results relate only to the items tested.

Page 9 of 12

### BT Environmental Consulting

Attention: James K. Sharp

Client Project #: 10-3997.00
P.O. #: Project name: GM-BEDFORD



### Quality Assurance Report

Maxxam Job Number: GB0B9532

QA/QC Date

Batch Analyzed

Num Init QC Type Parameter yyyy/mm/dd Value %Recovery Units QC Limits

2252937 AGE Spiked Blank 4-Bromofluorobenzene 2010/09/03 103 % 76 - 120 D4-1,2-Dichloroethane 2010/09/03 106 % 67 - 122

D8-Toluene 2010/09/03 101 % 75 - 114

Trichlorofluoromethane (FREON 11) 2010/09/03 104 % 70 - 130 1,1-Dichloroethylene 2010/09/03 102 % 70 - 130
Carbon Disulfide 2010/09/03 136 % N/A Methylene Chloride(Dichloromethane) 2010/09/03 110 % 70 - 130 1,1-Dichloroethane 2010/09/03 105 % 70 - 130 trans-1,2-Dichloroethylene 2010/09/03 101 % 70 - 130
Chloroform 2010/09/03 104 % 70 - 130 1,2-Dichloroethane 2010/09/03 110 % 70 - 130 1,1,1-Trichloroethane 2010/09/03 110 % 70 - 130
Carbon Tetrachloride 2010/09/03 116 % 70 - 130

Benzene 2010/09/03 104 % 70 - 130 1,1,2-Trichloroethane 2010/09/03 99 % 70 - 130 1,2-Dichloropropane 2010/09/03 109 % 70 - 130 Trichloroethylene 2010/09/03 99 % 70 - 130

Dibromomethane 2010/09/03 104 % N/A

Bromodichloromethane 2010/09/03 107 % 70 - 130 cis-1,3-Dichloropropene 2010/09/03 114 % 70 - 130 trans-1,3-Dichloropropene 2010/09/03 112 % 70 - 130

Dibromochloromethane 2010/09/03 108 % 70 - 130

Toluene 2010/09/03 103 % 70 - 130 Tetrachloroethylene 2010/09/03 100 % 70 - 130 Acrylonitrile 2010/09/03 113 % N/A

Method Blank 4-Bromofluorobenzene 2010/09/03 92 % 76 - 120

D4-1,2-Dichloroethane 2010/09/03 108 % 67 - 122

D8-Toluene 2010/09/03 104 % 75 - 114

Trichlorofluoromethane (FREON 11) 2010/09/03 ND, RDL=2.0 ug/L 1,1-Dichloroethylene 2010/09/03 ND, RDL=1.0 ug/L

Carbon Disulfide 2010/09/03 ND, RDL=0.50 ug/L Methylene Chloride(Dichloromethane) 2010/09/03 ND, RDL=1.0 ug/L 1,1-Dichloroethane 2010/09/03 ND, RDL=0.40 ug/L trans-1,2-Dichloroethylene 2010/09/03 ND, RDL=1.0 ug/L

Chloroform 2010/09/03 ND, RDL=0.40 ug/L 1,2-Dichloroethane 2010/09/03 ND, RDL=0.50 ug/L 1,1,1-Trichloroethane 2010/09/03 ND, RDL=0.50 ug/L

Carbon Tetrachloride 2010/09/03 ND, RDL=0.50 ug/L

Benzene 2010/09/03 ND, RDL=0.50 ug/L 1,1,2-Trichloroethane 2010/09/03 ND, RDL=0.50 ug/L 1,2-Dichloropropane 2010/09/03 ND, RDL=0.50 ug/L Trichloroethylene 2010/09/03 ND, RDL=0.50 ug/L

Dibromomethane 2010/09/03 ND, RDL=0.50 ug/L

Bromodichloromethane 2010/09/03 ND, RDL=0.40 ug/L cis-1,3-Dichloropropene 2010/09/03 ND, RDL=0.40 ug/L trans-1,3-Dichloropropene 2010/09/03 ND, RDL=0.60 ug/L

Dibromochloromethane 2010/09/03 ND, RDL=0.40 ug/L

Toluene 2010/09/03 ND, RDL=0.50 ug/L Tetrachloroethylene 2010/09/03 ND, RDL=0.50 ug/L Acrylonitrile 2010/09/03 ND, RDL=5.0 ug/L

2253781 YYA Spiked Blank Bromofluorobenzene 2010/09/01 101 % 36 - 141 D10-Ethylbenzene (FS) 2010/09/01 107 % 54 - 152 D4-1,2-Dichloroethane 2010/09/01 109 % 74 - 122

D8-Toluene 2010/09/01 97 % 80 - 114

Trichlorofluoromethane (FREON 11) 2010/09/01 122 % 50 - 150

Page 10 of 12

### BT Environmental Consulting

Attention: James K. Sharp

Client Project #: 10-3997.00
P.O. #: Project name: GM-BEDFORD



### Quality Assurance Report

(Continued)

Maxxam Job Number: GB0B9532

QA/QC Date

Batch Analyzed

Num Init QC Type Parameter yyyy/mm/dd Value %Recovery Units QC Limits

2253781 YYA Spiked Blank 1,1-Dichloroethylene 2010/09/01 104 % 50 - 150
Carbon Disulfide 2010/09/01 113 % 50 - 150 Methylene Chloride(Dichloromethane) 2010/09/01 87 % 50 - 150 1,1-Dichloroethane 2010/09/01 98 % 50 - 150 trans-1,2-Dichloroethylene 2010/09/01 95 % 50 - 150
Chloroform 2010/09/01 107 % 50 - 150 1,2-Dichloroethane 2010/09/01 105 % 50 - 150 1,1,1-Trichloroethane 2010/09/01 103 % 50 - 150
Carbon Tetrachloride 2010/09/01 107 % 50 - 150

Benzene 2010/09/01 94 % 50 - 150 1,1,2-Trichloroethane 2010/09/01 95 % 50 - 150 1,2-Dichloropropane 2010/09/01 96 % 50 - 150 Trichloroethylene 2010/09/01 95 % 50 - 150

Dibromomethane 2010/09/01 98 % 50 - 150

Bromodichloromethane 2010/09/01 102 % 50 - 150 cis-1,3-Dichloropropene 2010/09/01 99 % 50 - 150 trans-1,3-Dichloropropene 2010/09/01 102 % 50 - 150

Dibromochloromethane 2010/09/01 105 % 50 - 150

Toluene 2010/09/01 95 % 50 - 150 Tetrachloroethylene 2010/09/01 97 % 50 - 150 Acrylonitrile 2010/09/01 99 % N/A Chloroprene 2010/09/01 126 % N/A

Method Blank Bromofluorobenzene 2010/09/01 91 % 36 - 141

D10-Ethylbenzene (FS) 2010/09/01 100 % 54 - 152 D4-1,2-Dichloroethane 2010/09/01 111 % 74 - 122

D8-Toluene 2010/09/01 99 % 80 - 114

Trichlorofluoromethane (FREON 11) 2010/09/01 ND, RDL=0.01 ug 1,1-Dichloroethylene 2010/09/01 ND, RDL=0.01 ug Carbon Disulfide 2010/09/01 ND, RDL=0.03 ug Methylene Chloride(Dichloromethane) 2010/09/01 ND, RDL=0.02 ug 1,1-Dichloroethane 2010/09/01 ND, RDL=0.01 ug trans-1,2-Dichloroethylene 2010/09/01 ND, RDL=0.01 ug Chloroform 2010/09/01 ND, RDL=0.01 ug 1,2-Dichloroethane 2010/09/01 ND, RDL=0.007 ug 1,1,1-Trichloroethane 2010/09/01 ND, RDL=0.01 ug Carbon Tetrachloride 2010/09/01 ND, RDL=0.02 ug Benzene 2010/09/01 ND, RDL=0.009 ug 1,1,2-Trichloroethane 2010/09/01 ND, RDL=0.02 ug 1,2-Dichloropropane 2010/09/01 ND, RDL=0.01 ug Trichloroethylene 2010/09/01 ND, RDL=0.01 ug Dibromomethane 2010/09/01 ND, RDL=0.01 ug Bromodichloromethane 2010/09/01 ND, RDL=0.01 ug cis-1,3-Dichloropropene 2010/09/01 ND, RDL=0.01 ug trans-1,3-Dichloropropene 2010/09/01 ND, RDL=0.007 ug Dibromochloromethane 2010/09/01 ND, RDL=0.009 ug Toluene 2010/09/01 ND, RDL=0.01 ug Tetrachloroethylene 2010/09/01 ND, RDL=0.02 ug Acrylonitrile 2010/09/01 ND, RDL=0.03 ug Chloroprene 2010/09/01 ND, RDL=0.03 ug
2254579 YYA Spiked Blank Bromofluorobenzene 2010/09/02 100 % 36 - 141 D10-Ethylbenzene (FS) 2010/09/02 104 % 54 - 152 D4-1,2-Dichloroethane 2010/09/02 108 % 74 - 122

D8-Toluene 2010/09/02 97 % 80 - 114

Trichlorofluoromethane (FREON 11) 2010/09/02 118 % 50 - 150 1,1-Dichloroethylene 2010/09/02 100 % 50 - 150

Page 11 of 12

### BT Environmental Consulting

Attention: James K. Sharp

Client Project #: 10-3997.00
P.O. #: Project name: GM-BEDFORD



### Quality Assurance Report

(Continued)

Maxxam Job Number: GB0B9532

QA/QC Date

Batch Analyzed

Num Init QC Type Parameter yyyy/mm/dd Value %Recovery Units QC Limits

2254579 YYA Spiked Blank Carbon Disulfide 2010/09/02 111 % 50 - 150 Methylene Chloride(Dichloromethane) 2010/09/02 86 % 50 - 150 1,1-Dichloroethane 2010/09/02 96 % 50 - 150 trans-1,2-Dichloroethylene 2010/09/02 95 % 50 - 150
Chloroform 2010/09/02 106 % 50 - 150 1,2-Dichloroethane 2010/09/02 101 % 50 - 150 1,1,1-Trichloroethane 2010/09/02 100 % 50 - 150
Carbon Tetrachloride 2010/09/02 104 % 50 - 150

Benzene 2010/09/02 94 % 50 - 150 1,1,2-Trichloroethane 2010/09/02 91 % 50 - 150 1,2-Dichloropropane 2010/09/02 94 % 50 - 150 Trichloroethylene 2010/09/02 94 % 50 - 150

Dibromomethane 2010/09/02 94 % 50 - 150

Bromodichloromethane 2010/09/02 100 % 50 - 150 cis-1,3-Dichloropropene 2010/09/02 96 % 50 - 150 trans-1,3-Dichloropropene 2010/09/02 99 % 50 - 150

Dibromochloromethane 2010/09/02 100 % 50 - 150

Toluene 2010/09/02 92 % 50 - 150 Tetrachloroethylene 2010/09/02 94 % 50 - 150 Acrylonitrile 2010/09/02 96 % N/A Chloroprene 2010/09/02 119 % N/A

Method Blank Bromofluorobenzene 2010/09/02 95 % 36 - 141

D10-Ethylbenzene (FS) 2010/09/02 108 % 54 - 152 D4-1,2-Dichloroethane 2010/09/02 111 % 74 - 122

D8-Toluene 2010/09/02 97 % 80 - 114

Trichlorofluoromethane (FREON 11) 2010/09/02 ND, RDL=0.01 ug 1,1-Dichloroethylene 2010/09/02 ND, RDL=0.01 ug Carbon Disulfide 2010/09/02 ND, RDL=0.03 ug Methylene Chloride(Dichloromethane) 2010/09/02 ND, RDL=0.02 ug 1,1-Dichloroethane 2010/09/02 ND, RDL=0.01 ug trans-1,2-Dichloroethylene 2010/09/02 ND, RDL=0.01 ug Chloroform 2010/09/02 ND, RDL=0.01 ug 1,2-Dichloroethane 2010/09/02 ND, RDL=0.007 ug 1,1,1-Trichloroethane 2010/09/02 ND, RDL=0.01 ug Carbon Tetrachloride 2010/09/02 ND, RDL=0.02 ug Benzene 2010/09/02 ND, RDL=0.009 ug 1,1,2-Trichloroethane 2010/09/02 ND, RDL=0.02 ug 1,2-Dichloropropane 2010/09/02 ND, RDL=0.01 ug Trichloroethylene 2010/09/02 ND, RDL=0.01 ug Dibromomethane 2010/09/02 ND, RDL=0.01 ug Bromodichloromethane 2010/09/02 ND, RDL=0.01 ug cis-1,3-Dichloropropene 2010/09/02 ND, RDL=0.01 ug trans-1,3-Dichloropropene 2010/09/02 ND, RDL=0.007 ug Dibromochloromethane 2010/09/02 ND, RDL=0.009 ug Toluene 2010/09/02 ND, RDL=0.01 ug Tetrachloroethylene 2010/09/02 ND, RDL=0.02 ug Acrylonitrile 2010/09/02 ND, RDL=0.03 ug Chloroprene 2010/09/02 ND, RDL=0.03 ug

Spiked Blank: A blank matrix to which a known amount of the analyte has been added. Used to evaluate analyte recovery. Method Blank: A blank matrix containing all reagents used in the analytical procedure. Used to identify laboratory contamination. Surrogate: A pure or isotopically labeled compound whose behavior mirrors the analytes of interest. Used to evaluate extraction efficiency.

Page 12 of 12

### Your Project #: 10-3997.00
Site: GM BEDFORD

Your C.O.C. #: N/A

Attention: James K. Sharp

BT Environmental Consulting

2615 Wolcott St. Ferndale, MI
USA 48220

Report Date: 2010/09/30

This report supersedes all previous reports with the same Maxxam job number



## CERTIFICATE

OF ANALYSIS

MAXXAM JOB #: B0C7291

Received: 2010/09/04, 12:00

Sample Matrix: Stack

Sampling Train

# Samples Received: 5

Date Date Method Analyses Quantity Extracted Analyzed Laboratory Method Reference

PAH's in MM5 SamplingTrains (CARB429mod) ( 1 ) 5 2010/09/15 2010/09/29 BRL SOP-00201 CARB429(ARBM1,M2)mod

* RPDs calculated using raw data. The rounding of final results may result in the apparent difference.

(1) This test was performed in Maxxam Mississauga under Maxxam Burlington SCC Accreditation



### Encryption

Key

Please direct all questions regarding this Certificate of Analysis to your Project Manager.

LINA BARRETO, Project Manager

Email: Lina.Barreto@maxxamanalytics.com

Phone# (905) 817-5700

==================================================================== Maxxam has procedures in place to guard against improper use of the electronic signature and have the required "signatories", as per section

5.10.2 of ISO/IEC 17025:2005(E), signing the reports. For Service Group specific validation please refer to the Validation Signature Page.

Total cover pages: 1

Maxxam Analytics International Corporation o/a Maxxam Analytics Burlington:5555 North Service Road, Burlington, Ontario L7L 5H7 Telephone(905) 332-8788 Fax(905) 332-9169

Page 1 of 8

### BT Environmental Consulting

Maxxam Job #: B0C7291 Client Project #: 10-3997.00 Report Date: 2010/09/30 Project name: GM BEDFORD



### SEMI-VOLATILE ORGANICS BY GC-MS (STACK SAMPLING TRAIN)

Maxxam ID H D 6 8 9 4 H

D 6 8 9 5 H

D 6 8 9 6 H

D 6 8 9 7 H

D 6 9 1 7 Sampling Date 2010/08/24 2010/08/24 2010/08/23 2010/08/24 2010/08/24

COC Number N/A N/A N/A N/A N/A

U n i t s TRAIN FIELD RUN RUN RUN RDL QC Batch

BLK-M0010 BLK-M0010-MECL2/MEOH 1-M0010 2-M0010 3-M0010

Acenaphthene ug ND ND 0.36 ND ND 0.10 2269704

Acenaphthylene ug ND ND 0.10 ND ND 0.10 2269704

Anthracene ug ND ND 0.30 ND ND 0.10 2269704

Benzo(a)anthracene ug ND ND ND ND ND 0.10 2269704

Benzo(a)pyrene ug ND ND ND ND ND 0.10 2269704

Benzo(b)fluoranthene ug ND ND ND ND ND 0.10 2269704

Benzo(g,h,i)perylene ug ND ND ND ND ND 0.10 2269704

Benzo(k)fluoranthene ug ND ND ND ND ND 0.10 2269704

Chrysene ug ND ND ND ND ND 0.10 2269704

Dibenz(a,h)anthracene ug ND ND ND ND ND 0.10 2269704

Fluoranthene ug ND ND 0.38 0.23 ND 0.10 2269704

Fluorene ug 0.14 ND 1.70 0.21 ND 0.10 2269704

Indeno(1,2,3-cd)pyrene ug ND ND ND ND ND 0.10 2269704

Naphthalene ug 0.35 ND 18.5 3.12 7.24 0.20 2269704

Phenanthrene ug 0.34 ND 4.39 0.65 0.44 0.10 2269704

Pyrene ug ND ND ND 0.31 ND 0.10 2269704

Surrogate Recovery (%)

D10-2-Methylnaphthalene % 82 72 82 84 76 2269704

D10-Anthracene % 88 60 88 88 84 2269704

D10-Fluoranthene % 102 96 98 100 96 2269704

D10-Fluorene (FS) % 81 80 87 85 84 2269704

D10-Phenanthrene % 94 88 94 94 90 2269704

D12-Benzo(a)anthracene % 98 100 42 ( 1 ) 46 (

1 ) 50 2269704

D12-Benzo(a)pyrene % 56 70 4.0 ( 1 ) 6.0 (

1 ) 0.00 (

1 ) 2269704

D12-Benzo(b)fluoranthene % 96 96 92 96 92 2269704

D12-Benzo(ghi)perylene % 108 106 96 112 100 2269704

D12-Benzo(k)fluoranthene % 88 88 82 84 82 2269704

D12-Chrysene % 92 94 88 88 88 2269704

D12-Indeno(1,2,3-cd)pyrene % 102 102 96 108 96 2269704

D12-Perylene % 80 80 4.0 ( 1 ) 6.0 (

1 ) 0.00 (

1 ) 2269704

D14-Dibenzo(a,h)anthracene % 106 106 94 106 96 2269704

ND = Not detected

N/A = Not Applicable

RDL = Reportable Detection Limit
QC Batch = Quality Control Batch ( 1 ) Recovery or RPD for this parameter is outside control limits. The overall quality control for this analysis meets acceptability criteria.

Page 2 of 8

### BT Environmental Consulting

Maxxam Job #: B0C7291 Client Project #: 10-3997.00 Report Date: 2010/09/30 Project name: GM BEDFORD



### SEMI-VOLATILE ORGANICS BY GC-MS (STACK SAMPLING TRAIN)

Maxxam ID H D 6 8 9 4 H

D 6 8 9 5 H

D 6 8 9 6 H

D 6 8 9 7 H

D 6 9 1 7 Sampling Date 2010/08/24 2010/08/24 2010/08/23 2010/08/24 2010/08/24

COC Number N/A N/A N/A N/A N/A

U n i t s TRAIN FIELD RUN RUN RUN RDL QC Batch

BLK-M0010 BLK-M0010-MECL2/MEOH 1-M0010 2-M0010 3-M0010

D14-Terphenyl (FS) % 106 111 109 109 108 2269704

D8-Acenaphthylene % 76 66 4.0 ( 1 ) 2.0 (

1 ) 2.0 (

1 ) 2269704

D8-Naphthalene % 80 70 76 80 70 2269704

N/A = Not Applicable

RDL = Reportable Detection Limit
QC Batch = Quality Control Batch ( 1 ) Recovery or RPD for this parameter is outside control limits. The overall quality control for this analysis meets acceptability criteria.

Page 3 of 8

### BT Environmental Consulting

Maxxam Job #: B0C7291 Client Project #: 10-3997.00 Report Date: 2010/09/30 Project name: GM BEDFORD



### Test Summary

Maxxam ID HD6894 Collected 2010/08/24 Sample ID TRAIN BLK-M0010 Shipped

Matrix Stack Sampling Train Received 2010/09/04

Test Description Instrumentation Batch Extracted Analyzed Analyst

PAH's in MM5 SamplingTrains (CARB429m GC /MS 2269704 2010/09/15 2010/09/29 JIW

Maxxam ID HD6895 Collected 2010/08/24 Sample ID FIELD BLK-M0010-FILT Shipped

Matrix Stack Sampling Train Received 2010/09/04

Test Description Instrumentation Batch Extracted Analyzed Analyst

PAH's in MM5 SamplingTrains (CARB429m GC /MS 2269704 2010/09/15 2010/09/29 JIW

Maxxam ID HD6896 Collected 2010/08/23 Sample ID RUN 1-M0010 Shipped

Matrix Stack Sampling Train Received 2010/09/04

Test Description Instrumentation Batch Extracted Analyzed Analyst

PAH's in MM5 SamplingTrains (CARB429m GC /MS 2269704 2010/09/15 2010/09/29 JIW

Maxxam ID HD6897 Collected 2010/08/24 Sample ID RUN 2-M0010 Shipped

Matrix Stack Sampling Train Received 2010/09/04

Test Description Instrumentation Batch Extracted Analyzed Analyst

PAH's in MM5 SamplingTrains (CARB429m GC /MS 2269704 2010/09/15 2010/09/29 JIW

Maxxam ID HD6917 Collected 2010/08/24 Sample ID RUN 3-M0010 Shipped

Matrix Stack Sampling Train Received 2010/09/04

Test Description Instrumentation Batch Extracted Analyzed Analyst

PAH's in MM5 SamplingTrains (CARB429m GC /MS 2269704 2010/09/15 2010/09/29 JIW

Page 4 of 8

### BT Environmental Consulting

Maxxam Job #: B0C7291 Client Project #: 10-3997.00 Report Date: 2010/09/30 Project name: GM BEDFORD

GENERAL COMMENTS

PAHMM5-TR(WS:2269704) 7,12-Dimethylbenzo(a)anthracene is above 25% RSD in initial calibration. No positive found for this compound.

9.10-Dimethylanthracene and 7,12-Dimethylbenzo(a)anthracene are above 25% RSD in continuing calibration.

The recovery of Benzo(a)pyrene was low in Spike.

Not calibrated for Benzo(b)Anthracene, Picene, Dibenzo(a,c) anthracene and Triphenylene. An estimated mdl for each of these compounds is 0.1ug.
Since Dibenzo(a,c) anthracene co-elutes with Dibenzo(a,h) anthracene and Triphenylene with Chrysene each would have a value below estimated

mdl. Benzo(b)Anthracene elutes after Benzo(a)Anthracene and Chysene. Picene elutes after Dibenzo(a,h) anthracene. Searched for ions specific to

these 2 compounds in the appropriate retention time range with no possible positives detected.

Samples extracted past method recommended hold time.

Sample HD6894-01: PAHMM5-TR(WS:2269704)

This sample was sent as 3x split, but extracted as 2X split. The recoveries of fileld spikes were recalculated.

Sample HD6895-01: PAHMM5-TR(WS:2269704)

This sample was sent as 3x split, but extracted as 2X split. The recoveries of fileld spikes were recalculated.

Sample HD6896-01: PAHMM5-TR(WS:2269704)

The recoveries of D12-Benzo(a)pyrene, D12-Perylene, D12-Benzo(a)anthracene and D8-Acenaphthylene were low.

This sample was sent as 3x split, but extracted as 2X split. The recoveries of fileld spikes were recalculated.

Sample HD6897-01: PAHMM5-TR(WS:2269704)

The recoveries of D12-Benzo(a)pyrene, D12-Perylene, D12-Benzo(a)anthracene and D8-Acenaphthylene were low.

This sample was sent as 3x split, but extracted as 2X split. The recoveries of fileld spikes were recalculated.

Sample HD6917-01: PAHMM5-TR(WS:2269704)

The recoveries of D12-Benzo(a)pyrene, D12-Perylene and D8-Acenaphthylene were low.

This sample was sent as 3x split, but extracted as 2X split. The recoveries of fileld spikes were recalculated.

Results relate only to the items tested.

Page 5 of 8

### BT Environmental Consulting

Attention: James K. Sharp

Client Project #: 10-3997.00
P.O. #: Project name: GM BEDFORD



### Quality Assurance Report

Maxxam Job Number: GB0C7291

QA/QC Date

Batch Analyzed

Num Init QC Type Parameter yyyy/mm/dd Value %Recovery Units QC Limits

2269704 JIW Spiked Blank D10-2-Methylnaphthalene 2010/09/28 88 % 50 - 150

Spiked Blank DUP D10-2-Methylnaphthalene 2010/09/29 86 % 50 - 150 Spiked Blank D10-Fluoranthene 2010/09/28 90 % 50 - 150 Spiked Blank DUP D10-Fluoranthene 2010/09/29 92 % 50 - 150 Spiked Blank D10-Phenanthrene 2010/09/28 88 % 50 - 150 Spiked Blank DUP D10-Phenanthrene 2010/09/29 88 % 50 - 150 Spiked Blank D12-Benzo(a)anthracene 2010/09/28 94 % 50 - 150 Spiked Blank DUP D12-Benzo(a)anthracene 2010/09/29 100 % 50 - 150 Spiked Blank D12-Benzo(a)pyrene 2010/09/28 56 % 50 - 150 Spiked Blank DUP D12-Benzo(a)pyrene 2010/09/29 80 % 50 - 150 Spiked Blank D12-Benzo(b)fluoranthene 2010/09/28 94 % 50 - 150 Spiked Blank DUP D12-Benzo(b)fluoranthene 2010/09/29 96 % 50 - 150 Spiked Blank D12-Benzo(ghi)perylene 2010/09/28 106 % 50 - 150 Spiked Blank DUP D12-Benzo(ghi)perylene 2010/09/29 112 % 50 - 150 Spiked Blank D12-Benzo(k)fluoranthene 2010/09/28 96 % 50 - 150 Spiked Blank DUP D12-Benzo(k)fluoranthene 2010/09/29 98 % 50 - 150 Spiked Blank D12-Chrysene 2010/09/28 102 % 50 - 150 Spiked Blank DUP D12-Chrysene 2010/09/29 108 % 50 - 150 Spiked Blank D12-Indeno(1,2,3-cd)pyrene 2010/09/28 102 % 50 - 150 Spiked Blank DUP D12-Indeno(1,2,3-cd)pyrene 2010/09/29 108 % 50 - 150 Spiked Blank D12-Perylene 2010/09/28 68 % 50 - 150 Spiked Blank DUP D12-Perylene 2010/09/29 92 % 50 - 150 Spiked Blank D14-Dibenzo(a,h)anthracene 2010/09/28 104 % 50 - 150 Spiked Blank DUP D14-Dibenzo(a,h)anthracene 2010/09/29 110 % 50 - 150 Spiked Blank D8-Acenaphthylene 2010/09/28 82 % 50 - 150 Spiked Blank DUP D8-Acenaphthylene 2010/09/29 80 % 50 - 150 Spiked Blank D8-Naphthalene 2010/09/28 88 % 50 - 150 Spiked Blank DUP D8-Naphthalene 2010/09/29 84 % 50 - 150 Spiked Blank Acenaphthene 2010/09/28 81 % 60 - 130 Spiked Blank DUP Acenaphthene 2010/09/29 80 % 60 - 130

RPD Acenaphthene 2010/09/29 1.2 % 50 Spiked Blank Acenaphthylene 2010/09/28 80 % 60 - 130 Spiked Blank DUP Acenaphthylene 2010/09/29 79 % 60 - 130

RPD Acenaphthylene 2010/09/29 1.3 % 50 Spiked Blank Anthracene 2010/09/28 62 % 60 - 130 Spiked Blank DUP Anthracene 2010/09/29 69 % 60 - 130

RPD Anthracene 2010/09/29 10.4 % 50 Spiked Blank Benzo(a)anthracene 2010/09/28 87 % 60 - 130 Spiked Blank DUP Benzo(a)anthracene 2010/09/29 92 % 60 - 130

RPD Benzo(a)anthracene 2010/09/29 6.2 % 50 Spiked Blank Benzo(a)pyrene 2010/09/28 48 ( 1 ) % 60 - 130 Spiked Blank DUP Benzo(a)pyrene 2010/09/29 66 % 60 - 130

RPD Benzo(a)pyrene 2010/09/29 33.0 % 50 Spiked Blank Benzo(b)fluoranthene 2010/09/28 89 % 60 - 130 Spiked Blank DUP Benzo(b)fluoranthene 2010/09/29 93 % 60 - 130

RPD Benzo(b)fluoranthene 2010/09/29 4.4 % 50 Spiked Blank Benzo(g,h,i)perylene 2010/09/28 92 % 60 - 130 Spiked Blank DUP Benzo(g,h,i)perylene 2010/09/29 97 % 60 - 130

RPD Benzo(g,h,i)perylene 2010/09/29 5.3 % 50 Spiked Blank Benzo(k)fluoranthene 2010/09/28 90 % 60 - 130 Spiked Blank DUP Benzo(k)fluoranthene 2010/09/29 93 % 60 - 130

RPD Benzo(k)fluoranthene 2010/09/29 3.6 % 50 Spiked Blank Chrysene 2010/09/28 96 % 60 - 130 Spiked Blank DUP Chrysene 2010/09/29 100 % 60 - 130

RPD Chrysene 2010/09/29 3.6 % 50

Maxxam Analytics International Corporation o/a Maxxam Analytics Burlington:5555 North Service Road, Burlington, Ontario L7L 5H7 Telephone(905) 332-8788 Fax(905) 332-9169

Page 6 of 8

### BT Environmental Consulting

Attention: James K. Sharp

Client Project #: 10-3997.00
P.O. #: Project name: GM BEDFORD



### Quality Assurance Report

(Continued)

Maxxam Job Number: GB0C7291

QA/QC Date

Batch Analyzed

Num Init QC Type Parameter yyyy/mm/dd Value %Recovery Units QC Limits

2269704 JIW Spiked Blank Dibenz(a,h)anthracene 2010/09/28 91 % 60 - 130

Spiked Blank DUP Dibenz(a,h)anthracene 2010/09/29 97 % 60 - 130

RPD Dibenz(a,h)anthracene 2010/09/29 6.9 % 50 Spiked Blank Fluoranthene 2010/09/28 86 % 60 - 130 Spiked Blank DUP Fluoranthene 2010/09/29 88 % 60 - 130

RPD Fluoranthene 2010/09/29 2.3 % 50 Spiked Blank Fluorene 2010/09/28 80 % 60 - 130 Spiked Blank DUP Fluorene 2010/09/29 79 % 60 - 130

RPD Fluorene 2010/09/29 0.9 % 50 Spiked Blank Indeno(1,2,3-cd)pyrene 2010/09/28 91 % 60 - 130 Spiked Blank DUP Indeno(1,2,3-cd)pyrene 2010/09/29 97 % 60 - 130

RPD Indeno(1,2,3-cd)pyrene 2010/09/29 6.1 % 50 Spiked Blank Naphthalene 2010/09/28 82 % 60 - 130 Spiked Blank DUP Naphthalene 2010/09/29 80 % 60 - 130

RPD Naphthalene 2010/09/29 3.4 % 50 Spiked Blank Phenanthrene 2010/09/28 81 % 60 - 130 Spiked Blank DUP Phenanthrene 2010/09/29 81 % 60 - 130

RPD Phenanthrene 2010/09/29 0.3 % 50 Spiked Blank Pyrene 2010/09/28 83 % 60 - 130 Spiked Blank DUP Pyrene 2010/09/29 86 % 60 - 130

RPD Pyrene 2010/09/29 3.6 % 50

Method Blank D10-2-Methylnaphthalene 2010/09/29 100 % 50 - 150

D10-Fluoranthene 2010/09/29 92 % 50 - 150

D10-Phenanthrene 2010/09/29 94 % 50 - 150 D12-Benzo(a)anthracene 2010/09/29 100 % 50 - 150 D12-Benzo(a)pyrene 2010/09/29 56 % 50 - 150 D12-Benzo(b)fluoranthene 2010/09/29 98 % 50 - 150 D12-Benzo(ghi)perylene 2010/09/29 112 % 50 - 150 D12-Benzo(k)fluoranthene 2010/09/29 96 % 50 - 150 D12-Chrysene 2010/09/29 106 % 50 - 150 D12-Indeno(1,2,3-cd)pyrene 2010/09/29 106 % 50 - 150 D12-Perylene 2010/09/29 76 % 50 - 150 D14-Dibenzo(a,h)anthracene 2010/09/29 108 % 50 - 150 D8-Acenaphthylene 2010/09/29 90 % 50 - 150 D8-Naphthalene 2010/09/29 100 % 50 - 150 Acenaphthene 2010/09/29 ND, RDL=0.10 ug Acenaphthylene 2010/09/29 ND, RDL=0.10 ug Anthracene 2010/09/29 ND, RDL=0.10 ug Benzo(a)anthracene 2010/09/29 ND, RDL=0.10 ug Benzo(a)pyrene 2010/09/29 ND, RDL=0.10 ug Benzo(b)fluoranthene 2010/09/29 ND, RDL=0.10 ug Benzo(g,h,i)perylene 2010/09/29 ND, RDL=0.10 ug Benzo(k)fluoranthene 2010/09/29 ND, RDL=0.10 ug Chrysene 2010/09/29 ND, RDL=0.10 ug Dibenz(a,h)anthracene 2010/09/29 ND, RDL=0.10 ug Fluoranthene 2010/09/29 ND, RDL=0.10 ug Fluorene 2010/09/29 ND, RDL=0.10 ug Indeno(1,2,3-cd)pyrene 2010/09/29 ND, RDL=0.10 ug Naphthalene 2010/09/29 ND, RDL=0.20 ug Phenanthrene 2010/09/29 ND, RDL=0.10 ug Pyrene 2010/09/29 ND, RDL=0.10 ug

Duplicate: Paired analysis of a separate portion of the same sample. Used to evaluate the variance in the measurement. Spiked Blank: A blank matrix to which a known amount of the analyte has been added. Used to evaluate analyte recovery. Method Blank: A blank matrix containing all reagents used in the analytical procedure. Used to identify laboratory contamination. Surrogate: A pure or isotopically labeled compound whose behavior mirrors the analytes of interest. Used to evaluate extraction efficiency.

Maxxam Analytics International Corporation o/a Maxxam Analytics Burlington:5555 North Service Road, Burlington, Ontario L7L 5H7 Telephone(905) 332-8788 Fax(905) 332-9169 Page 7 of 8

### BT Environmental Consulting

Attention: James K. Sharp

Client Project #: 10-3997.00
P.O. #: Project name: GM BEDFORD



### Quality Assurance Report

(Continued)

Maxxam Job Number: GB0C7291

QA/QC Date

Batch Analyzed

Num Init QC Type Parameter yyyy/mm/dd Value %Recovery Units QC Limits ( 1 ) Recovery or RPD for this parameter is outside control limits. The overall quality control for this analysis meets acceptability criteria.

Maxxam Analytics International Corporation o/a Maxxam Analytics Burlington:5555 North Service Road, Burlington, Ontario L7L 5H7 Telephone(905) 332-8788 Fax(905) 332-9169

Page 8 of 8

# Appendix E Example Calculations

## EXAMPLE CALCULATIONS

Note: answers obtained by sample calculations may deviate from that presented within the report because of rounding differences.

USEPA METHOD 1-4

Moisture Content

11 

## VKV

wc 

## ⋅=

22 

# VKV

wsg 

# ⋅=

Where: V

wc 

## = volume of water vapor condensed in impingers at standard conditions (ft 3 

## )

K 1 

## = 0.04715 ft 3 

## /g water

V 1 

## = mass of water collected in impingers (g)

V wsg 

## = volume of water vapor collected in silica gel at standard conditions (ft 3 

## )

K 2 

## = 0.04715 ft 3 

## /g water

V 2 

## = mass of water collected by silica gel (g)

For example, for Run 1 (P-1) of the 0010 testing at the Aluminum Chip Dryer, 780 g of water were condensed in the impingers, and 52 g of water were collected by the silica gel.

The volume of water collected in each section of the sampling train, in ft 3 

## , was calculated

as follows:



# ( ) 3 

## ft 777.36g 807
g ft 04715.0 = ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛

= wc 

## V 3



# ( ) 3 3 

## ft 4518.252g ft 04715.0 = ⎟ ⎟ ⎞ ⎜ ⎜ ⎛

= V
g ⎠ ⎝ wsg



## The total volume of water collected was 36.777 ft 3 

## + 2.4518 ft 3 

## = 39.23 ft 3



## .

## Gas Volume Standardization



# ⎟ ⎟ ⎟ ⎟

⎠ ⎞

⎜ ⎜ ⎜ ⎜

⎝ ⎛ Δ
+ ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛

=

m b

std std

mmstd 

# T H P

P T YVV 6.13

Where: V std 

## = volume of gas sampled at standard conditions

V

m 

## = volume of gas measured by dry gas meter (ft 3 

## )

Y

m 

## = dry gas meter correction factor (dimensionless)

T std 

## = standard temperature ( o 

## R = 460 + o 

## F)

P std 

## = standard pressure (“Hg)

P b 

## = barometric pressure (“Hg)



# Δ H = average orifice differential pressure (“H 2 

## O)

T

m 

## = average meter temperature ( o 

## R)

For example, the volume of gas measured at the dry gas meter for Run 1 of the 0010 testing at the Aluminum Chip Dryer was 164.48 ft 3 

## . The dry gas meter correction factor was 1.013. Standard temperat ure and pressure are 530 o 

## R and 29.92”Hg, respectively. The barometric pressure at the time of testing was 29.98”Hg. The average orifice differential, and meter temperature were 2.29 and 561.6 o 

## R, respectively. The volume of gas sampled was corrected to standard conditions as follows:



# ( ) ( ) standard ,ft 44.158 6.561 Hg" OH" 6.13 OH2.29" Hg9.98"2

Hg" 92.29

530 013.1ft 64.481 3

o 2 2

3



# =

⎟ ⎟ ⎟ ⎟ ⎟ ⎟ ⎟

⎠ ⎞

⎜ ⎜ ⎜ ⎜ ⎜ ⎜ ⎜

⎝ ⎛

+

⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛

= R R V o

std



## Moisture Fraction

std wsg wc wsg wc

ws 

## VVV VV B

++ +

=



## Where: B

ws 

## = exhaust gas moisture content

For example, from previously calculated va lues, the exhaust gas moisture fraction for Run 1 of the 0010 testing at the Aluminum Chip Dryer was calculated as follows:



# %85.19 158.44f t f t 39.23 ft23.39

3 3 3



# =

+ = B

ws

# Absolute Stack Gas Temperature, T

s 

# ( o 

# R)

s s 

# tT += 460

Where: t

s 

# = Measured stack gas temperature ( o 

# F)

For example, for Run 1 of the 0010 testing at the Aluminum Chip Dryer, the average stack temperature was 310.30 o 

# F. The average temperature in degrees Rankine is

therefore 310.30 + 459.59 = 769.97 o 

# R.

Absolute Stack Gas Pressure, P

s 

# (in. Hg)



# ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

+= 6.13 stat
bars 

# P PP

Where: P bar 

# = Barometric pressure at test site (in. Hg)

P stat 

# = Stack static pressure (in. Hg)

For example, for Run 1 of the 0010 testing at the Aluminum Chip Dryer, the barometric and stack static pressures were 29.98”Hg, and -0.17” H 2 

# O, respectively. The absolute stack pressure is then:

Hg P

s 

## "98.29 6.13 17.0 98.29 = ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

− +=



# Stack Gas Molecular Weight, Dry Basis (lb/lb mole)



# )%(%28.0)(%32.0)(%44.0 2 2 2 

# CON O CO M d 

# + + + =

For example, for Run 1 of the 0010 testing at the Aluminum Chip Dryer, the average O 2 

# content of the exhaust gas stream was 16.5% (from Orsat). The CO 2 

# content of the gas stream was 2.5% (from Orsat). The CO cont ent was assumed to be negligible, and the N 2 

# content is assumed to make up the balance of the gas content (i.e. 100-19.0 = 81.0%). The dry stack gas molecular weight is therefore:



# mollb lb 06.29%)0.81(28.0%)5.2(32.0%)5.16(44.0 = + + = d 

# M

# Stack Gas Molecular Weight, Wet Basis (lb/lb mole)



# ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

+ ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

−= 100 18 100 1 ws ws ds 

# BB MM

The stack gas moisture content for Run 1 of the 0010 testing at the Aluminum Chip Dryer was 19.85%. The wet stack gas molecular weight is then:



# mol lb lb 86.26 100 85.19 18 100 85.19 1 mol lb lb 06.29 = ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

+ ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

− = s 

# M

Stack Gas Velocity, V

s 

# (fpm)

ss

s

pp s 

# MP T PCK V Δ ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

= min sec 60

Where: K p 

# = Pitot tube cons tant equal to 85.49 ).)(( ).)(/(

sec 2 

## OHinR Hginmolelblbft

o 

## ⋅



# C p 

# = Pitot tube coefficient, dimensionless

Δ P = The average square root of the velocity head of stack gas (in. H 2 

# O)

M
s 

# = Molecular weight of the stack gas, wet basis (lb/lb mole)

For example, for Run 1 of the 0010 testing at the Aluminum Chip Dryer, the average square root of the velocity h ead of the stack gas was 0.281”H 2 

# O. Using values already calculated, the average stack gas velocity was calculated as follows:



# ( ) ( ) 

# ( ) ( ) ( )



# ( )

( ) min 51.1202

mol lb lb 86.26.06.29 97.769 .281.0 84.0

. .mol lb/lb

sec 49.85 min sec 60

2



# ft

Hgin R Hgin OHinR Hgin ft V

o o s



# = ⎟ ⎠ ⎞ ⎜ ⎝ ⎛ ⋅ ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛ ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

=

# Average Stack Gas Volumetric Flowrate, Q

s 

# (cfm)

AVQ

ss



## ⋅=



# Where: V

s 

# = Stack gas velocity (fpm)
A = Cross-sectional area of stack (ft 2 

# )

For example, the Aluminum Chip Dryer has a 60 inch diameter. The cross-sectional area

of the stack is calculated as follows:

3 2 

# 63.19 12 60 4 ft in ft in = ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

∗ π

For Run 1 of the 0010 testing at the Alumin um Chip Dryer, the stack gas volumetric

flowrate was then calculated as follows:



# ( )

min 605,2363.19 min 202,1 3

2 

## ft ft ft Q

s 

## = ⋅ ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

=



## Standard Stack Gas Volumetric Flowrate, Q std 

## (scfm)



# ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛ ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛

= Hgin P

T R QQ s

s o

sstd 

# .92.29 530

Where: T

s 

# = Absolute stack gas temperature ( o 

# R)

P
s 

# = Absolute stack gas pressure (in. Hg)

For example, for Run 1 of the 0010 testing at the Aluminum Chip Dryer, the standard stack gas volumetric flowrate was calculated as follows:



# standard, min 281,16 .92.29 ..98.29

97.769

530

min 605,23 3 3 

# ft

Hgin Hgin

R R ft Q

o o

std 

# = ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛ ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛

=

# Dry Standard Stack Gas Volumetric Flowrate, Q std,dry 

# (dscfm)



# ( )

ws std drystd 

# BQQ −= 

# 1

,



# For example, for Run 1 of the 0010 testing at the Aluminum Chip Dryer, the dry standard stack gas volumetric flowrate was calculated as follows:



# ( ) dry standard, mi n 049,131985.1standard, mi n 281,16 3 3

, 

# ft ft Q drystd 

# =− =



# Mass Emission Rate (kg/hr)

⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛ ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

=

mstd drystd 

## V M

hr Q min 60 Rate Emission

,



# Where: Q std,dry 

# = dry standard stack ga s volumetric flowrate (ft 3 

# /min). M = mass from laboratory test results for desired compound (μg)

V mstd 

# = dry gas meter volume sampled

The dry standard flowrate for Run 1 of the 0031 testing at the Aluminum Chip Dryer was 13,049 ft 3 

# /min. Laboratory results for Misc Organi cs emissions returned a 0.08μg result. The mass loading in kilograms per hour is then:

hr kg

g kg

stdft g

hr ft 7

9 3 3 

## 10*63.8 10 6.71 08.0min 60 min 879,12Rate Emission

− 

## = ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛ ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎝ ⎛ ⎟ ⎠ ⎞ ⎜ ⎝ ⎛

= μ μ



# Feed Rate Emissions (kg pollution / Mg feed)

Emissions Rate feed 

# FeedRate te EmissionRa

=



# The Aluminum Chip Dryer process had a feed rate of 11,849 lb/hr during the course of Run 1 of the 0031 testing. Using the Emission Rate calculated above we are able to generate an emissions rate in relation to the amount of mass fed through the process.

Mg kg

lb Mg

hr lb hr kg

ate EmissionsR feed 7 7



# 10*61.1

62.204,2 *849,11 10*63.8

− −



# = ⎟ ⎠ ⎞ ⎜ ⎝ ⎛ =

# Appendix F

Production DataAfter BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/23 16:49:00 1410 11877 2975 558 1 1 0 2.1 1410 1405 82211 11524 173935 11676 2.02010/08/23 16:50:00 1411 11742 2710 558 1 1 0 1.7 1410 1405 82258 11533 174130 11676 2.02010/08/23 16:51:00 1405 11872 3051 558 1 1 0 2.6 1409 1405 82307 11543 174327 11676 2.02010/08/23 16:52:00 1399 11968 3659 558 1 1 0 3.0 1408 1405 82364 11552 174529 11716 2.12010/08/23 16:53:00 1403 11151 3442 558 1 1 0 2.6 1407 1405 82424 11561 174728 11716 2.12010/08/23 16:54:00 1411 12140 2774 558 1 1 0 3.1 1407 1405 82475 11571 174927 11716 2.22010/08/23 16:55:00 1417 12176 2006 554 1 1 0 2.9 1408 1405 82513 11580 175129 11774 2.32010/08/23 16:56:00 1418 12203 1581 558 1 1 0 3.5 1408 1405 82542 11589 175332 11774 2.32010/08/23 16:57:00 1403 10851 2872 562 1 1 0 2.8 1408 1405 82579 11599 175529 11774 2.32010/08/23 16:58:00 1392 11613 4006 562 1 1 0 2.3 1407 1405 82638 11608 175729 11842 2.32010/08/23 16:59:00 1393 12421 3960 560 1 1 0 1.4 1406 1405 82706 11617 175928 11842 2.32010/08/23 17:00:00 1404 11970 3460 560 1 1 0 1.7 1405 1405 82768 11627 176131 11842 2.32010/08/23 17:01:00 1410 11686 2593 562 1 1 0 1.1 1406 1405 82816 11636 176334 11890 2.22010/08/23 17:02:00 1415 12600 2046 562 1 1 0 1.5 1406 1405 82854 11645 176535 11890 2.22010/08/23 17:03:00 1413 12517 1957 562 1 1 0 1.6 1407 1405 82887 11655 176739 11890 2.22010/08/23 17:04:00 1407 12160 2633 562 1 1 0 1.6 1407 1405 82925 11664 176946 11943 2.22010/08/23 17:05:00 1400 11631 3092 562 1 1 0 1.9 1407 1405 82973 11673 177148 11943 2.22010/08/23 17:06:00 1401 11715 3202 562 1 1 0 2.0 1406 1405 83027 11683 177346 11943 2.22010/08/23 17:07:00 1410 12003 2364 558 1 1 0 2.3 1406 1405 83074 11692 177543 11982 2.12010/08/23 17:08:00 1414 11555 1921 547 1 1 0 2.8 1407 1405 83109 11701 177742 11982 2.12010/08/23 17:09:00 1412 12089 2002 562 1 1 0 3.0 1408 1405 83140 11711 177947 11982 2.22010/08/23 17:10:00 1407 12611 1993 558 1 1 0 2.9 1407 1406 83174 11720 178154 11987 2.12010/08/23 17:11:00 1405 13022 2527 562 1 1 0 3.1 1407 1406 83215 11730 178363 11987 2.12010/08/23 17:12:00 1424 12596 1049 558 1 1 0 2.8 1407 1406 83244 11739 178574 11987 2.12010/08/23 17:13:00 1437 12675 1213 562 1 1 0 2.8 1409 1406 83262 11748 178785 11995 2.22010/08/23 17:14:00 1438 12687 1065 562 1 1 0 2.4 1412 1406 83279 11758 178997 11995 2.22010/08/23 17:15:00 1428 12962 1032 562 1 1 0 2.7 1414 1406 83297 11767 179206 11995 2.32010/08/23 17:16:00 1395 12418 3199 562 1 1 0 2.1 1415 1406 83325 11776 179417 11988 2.42010/08/23 17:17:00 1382 12400 4809 558 1 1 0 2.3 1413 1406 83396 11786 179627 11988 2.42010/08/23 17:18:00 1393 13585 3830 560 1 1 0 2.9 1411 1406 83471 11795 179838 11988 2.52010/08/23 17:19:00 1411 13599 2551 558 1 1 0 3.0 1410 1406 83525 11804 180063 11975 2.52010/08/23 17:20:00 1421 14165 1416 558 1 1 0 2.6 1411 1406 83555 11814 180298 11975 2.62010/08/23 17:21:00 1415 13599 1378 556 1 1 0 1.9 1412 1406 83576 11823 180527 11975 2.62010/08/23 17:22:00 1406 12907 2330 558 1 1 0 1.6 1412 1406 83608 11832 180745 11960 2.62010/08/23 17:23:00 1401 12538 2924 558 1 1 0 1.9 1412 1406 83652 11841 180958 11960 2.62010/08/23 17:24:00 1401 11702 2999 558 1 1 0 1.6 1411 1406 83702 11851 181168 11960 2.52010/08/23 17:25:00 1409 11865 2093 560 1 1 0 2.1 1411 1406 83746 11860 181374 11957 2.42010/08/23 17:26:00 1417 12265 1453 558 1 1 0 2.9 1411 1406 83776 11869 181577 11957 2.42010/08/23 17:27:00 1414 11789 1587 572 1 1 0 3.0 1411 1406 83795 11879 181777 11957 2.42010/08/23 17:28:00 1405 11946 2314 560 1 1 0 2.6 1410 1406 83826 11888 181980 11921 2.42010/08/23 17:29:00 1412 12273 1767 558 1 1 0 2.8 1408 1406 83865 11897 182191 11921 2.42010/08/23 17:30:00 1434 12850 923 558 1 1 0 2.3 1407 1406 83883 11907 182403 11921 2.42010/08/23 17:31:00 1436 13912 942 558 1 1 0 2.5 1409 1407 83901 11916 182620 11928 2.42010/08/23 17:32:00 1425 12826 1065 560 1 1 0 2.4 1412 1407 83918 11925 182838 11928 2.42010/08/23 17:33:00 1392 12323 3083 562 1 1 0 2.6 1414 1407 83946 11935 183050 11928 2.42010/08/23 17:34:00 1380 12150 4594 562 1 1 0 2.9 1412 1407 84015 11944 183258 11938 2.4Run 1After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/23 17:35:00 1394 13131 3757 560 1 1 0 2.1 1410 1407 84087 11953 183468 11938 2.42010/08/23 17:36:00 1413 12744 2168 560 1 1 0 1.6 1409 1407 84135 11963 183685 11938 2.42010/08/23 17:37:00 1429 13064 799 563 1 1 0 1.5 1410 1407 84156 11972 183909 11949 2.42010/08/23 17:38:00 1428 13554 1057 563 1 1 0 1.7 1412 1407 84173 11982 184133 11949 2.42010/08/23 17:39:00 1417 12667 1318 562 1 1 0 2.7 1413 1407 84191 11991 184346 11949 2.42010/08/23 17:40:00 1402 11912 2969 563 1 1 0 2.8 1414 1407 84229 12000 184551 11936 2.52010/08/23 17:41:00 1401 12107 3246 565 1 1 0 2.8 1412 1407 84282 12010 184752 11936 2.52010/08/23 17:42:00 1410 12494 2188 565 1 1 0 2.7 1412 1407 84326 12019 184956 11936 2.42010/08/23 17:43:00 1419 12477 1082 565 1 1 0 2.2 1412 1407 84352 12028 185159 11921 2.42010/08/23 17:44:00 1417 12186 1221 565 1 1 0 2.3 1413 1407 84369 12038 185363 11921 2.42010/08/23 17:45:00 1405 12337 2430 563 1 1 0 3.3 1412 1407 84397 12047 185562 11921 2.42010/08/23 17:46:00 1399 12785 3100 562 1 1 0 2.7 1410 1407 84445 12057 185766 11885 2.52010/08/23 17:47:00 1421 13135 1032 565 1 1 0 2.1 1408 1407 84481 12066 185976 11885 2.42010/08/23 17:48:00 1424 13098 1228 563 1 1 0 1.4 1409 1407 84498 12075 186189 11885 2.42010/08/23 17:49:00 1406 12442 2076 558 1 1 0 2.7 1412 1407 84520 12085 186400 11895 2.32010/08/23 17:50:00 1390 13068 3788 565 1 1 0 3.0 1412 1407 84571 12094 186609 11895 2.32010/08/23 17:51:00 1391 12880 3937 563 1 1 0 2.6 1411 1407 84635 12103 186815 11895 2.42010/08/23 17:52:00 1405 12463 2762 562 1 1 0 2.4 1410 1407 84690 12113 187022 11886 2.52010/08/23 17:53:00 1415 13136 1757 560 1 1 0 2.3 1409 1407 84727 12122 187237 11886 2.52010/08/23 17:54:00 1412 12877 1581 560 1 1 0 2.2 1408 1407 84752 12132 187453 11886 2.52010/08/23 17:55:00 1399 13631 2915 562 1 1 0 2.2 1408 1407 84790 12141 187665 11881 2.52010/08/23 17:56:00 1391 12159 3786 562 1 1 0 2.4 1408 1407 84848 12150 187874 11881 2.42010/08/23 17:57:00 1394 12384 3864 560 1 1 0 2.3 1407 1407 84911 12160 188084 11881 2.42010/08/23 17:58:00 1404 12152 3086 560 1 1 0 2.2 1406 1407 84968 12169 188287 11898 2.42010/08/23 17:59:00 1410 12662 2244 560 1 1 0 2.5 1405 1407 85012 12178 188492 11898 2.42010/08/23 18:00:00 1409 12085 2283 586 1 1 0 2.4 1404 1407 85051 12188 188696 11898 2.42010/08/23 18:01:00 1403 12301 2912 560 1 1 0 2.3 1405 1407 85095 12197 188897 11894 2.32010/08/23 18:02:00 1398 12279 3411 563 1 1 0 2.1 1404 1407 85147 12207 189100 11894 2.32010/08/23 18:03:00 1398 12244 3439 562 1 1 0 2.4 1402 1407 85205 12216 189302 11894 2.32010/08/23 18:04:00 1405 12087 2859 562 1 1 0 2.0 1401 1407 85259 12225 189506 11905 2.32010/08/23 18:05:00 1410 12041 2430 560 1 1 0 1.8 1402 1407 85302 12235 189708 11905 2.32010/08/23 18:06:00 1406 11763 2589 567 1 1 0 2.4 1403 1407 85343 12244 189907 11905 2.32010/08/23 18:07:00 1402 12144 3025 563 1 1 0 2.7 1403 1407 85390 12253 190104 11909 2.22010/08/23 18:08:00 1398 11966 3445 563 1 1 0 2.9 1403 1407 85443 12263 190305 11909 2.32010/08/23 18:09:00 1394 12704 3783 563 1 1 0 2.9 1401 1407 85501 12272 190513 11909 2.32010/08/23 18:10:00 1399 12869 3623 565 1 1 0 2.0 1401 1407 85562 12282 190723 11923 2.42010/08/23 18:11:00 1408 12700 2749 563 1 1 0 2.6 1401 1407 85614 12291 190934 11923 2.42010/08/23 18:12:00 1405 11957 2816 567 1 1 0 2.7 1403 1407 85656 12300 191135 11923 2.42010/08/23 18:13:00 1395 12160 3681 560 1 1 0 2.6 1403 1407 85709 12310 191344 11944 2.32010/08/23 18:14:00 1394 12539 3989 563 1 1 0 2.4 1402 1407 85774 12319 191547 11944 2.42010/08/23 18:15:00 1415 12291 2208 562 1 1 0 2.8 1401 1407 85828 12329 191750 11944 2.42010/08/23 18:16:00 1417 11933 1631 562 1 1 0 2.9 1403 1407 85851 12338 191949 11951 2.52010/08/23 18:17:00 1398 12285 3429 565 1 1 0 2.8 1403 1407 85894 12347 192153 11951 2.52010/08/23 18:18:00 1393 11820 3953 562 1 1 0 2.8 1403 1407 85956 12357 192353 11951 2.52010/08/23 18:19:00 1395 11928 3930 558 1 1 0 2.7 1402 1407 86022 12366 192552 11948 2.62010/08/23 18:20:00 1407 12105 3075 565 1 1 0 2.6 1402 1407 86081 12375 192751 11948 2.62010/08/23 18:21:00 1413 12494 2356 562 1 1 0 2.8 1402 1407 86125 12385 192955 11948 2.7After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/23 18:22:00 1412 11611 2405 558 1 1 0 1.0 1403 1407 86165 12394 193156 11955 2.72010/08/23 18:23:00 1405 11777 2948 562 1 1 0 2.2 1403 1407 86209 12404 193356 11955 2.62010/08/23 18:24:00 1410 11637 2680 563 1 1 0 1.5 1404 1407 86259 12413 193558 11955 2.52010/08/23 18:25:00 1427 11819 1074 562 1 1 0 1.6 1405 1407 86288 12422 193760 11938 2.52010/08/23 18:26:00 1423 11948 1065 565 1 1 0 2.4 1407 1407 86306 12432 193962 11938 2.42010/08/23 18:27:00 1397 12035 3257 562 1 1 0 1.8 1407 1407 86341 12441 194167 11938 2.42010/08/23 18:28:00 1384 11662 4947 562 1 1 0 2.8 1406 1407 86414 12450 194358 11932 2.42010/08/23 18:29:00 1394 12630 4295 562 1 1 0 2.6 1405 1407 86491 12460 194561 11932 2.42010/08/23 18:30:00 1410 12424 2890 567 1 1 0 2.2 1405 1407 86551 12469 194765 11932 2.42010/08/23 18:31:00 1418 12033 1989 565 1 1 0 1.8 1404 1407 86591 12479 194977 11958 2.32010/08/23 18:32:00 1412 12529 2371 565 1 1 0 1.6 1405 1407 86626 12488 195185 11958 2.22010/08/23 18:33:00 1397 12426 3485 562 1 1 0 1.6 1406 1407 86673 12497 195392 11958 2.12010/08/23 18:34:00 1389 12453 4326 567 1 1 0 1.9 1406 1407 86740 12507 195593 11968 2.12010/08/23 18:35:00 1394 12255 4094 563 1 1 0 1.6 1405 1407 86812 12516 195801 11968 2.02010/08/23 18:36:00 1399 12491 3603 565 1 1 0 1.7 1404 1407 86876 12526 196002 11968 1.92010/08/23 18:37:00 1404 11690 3289 562 1 1 0 2.0 1404 1407 86934 12535 196204 11966 1.92010/08/23 18:38:00 1402 11914 3297 565 1 1 0 2.3 1403 1407 86988 12544 196403 11966 1.92010/08/23 18:39:00 1397 11440 3853 562 1 1 0 2.0 1403 1407 87048 12554 196602 11966 2.02010/08/23 18:40:00 1409 11743 2984 565 1 1 0 2.9 1402 1406 87109 12563 196800 11965 2.02010/08/23 18:41:00 1416 12059 2097 563 1 1 0 3.1 1401 1406 87148 12573 197000 11965 2.12010/08/23 18:42:00 1402 11436 3257 562 1 1 0 2.9 1401 1406 87190 12582 197203 11965 2.22010/08/23 18:43:00 1383 12409 4882 565 1 1 0 2.9 1402 1406 87259 12591 197400 11941 2.22010/08/23 18:44:00 1387 11875 5025 563 1 1 0 2.6 1401 1406 87344 12601 197594 11941 2.32010/08/23 18:45:00 1392 11783 4676 562 1 1 0 3.2 1401 1406 87423 12610 197796 11941 2.22010/08/23 18:46:00 1407 12069 3667 563 1 1 0 2.4 1400 1406 87492 12619 197996 11940 2.32010/08/23 18:47:00 1418 12812 2375 562 1 1 0 3.3 1400 1406 87542 12629 198202 11940 2.42010/08/23 18:48:00 1412 12588 2736 563 1 1 0 3.0 1400 1406 87582 12638 198408 11940 2.42010/08/23 18:49:00 1392 11900 4403 562 1 1 0 2.9 1401 1406 87641 12648 198614 11938 2.52010/08/23 18:50:00 1383 11910 5340 565 1 1 0 2.7 1401 1406 87723 12657 198815 11938 2.62010/08/23 18:51:00 1382 11811 5569 565 1 1 0 3.0 1400 1406 87815 12666 199014 11938 2.62010/08/23 18:52:00 1390 11578 5113 563 1 1 0 3.5 1399 1406 87906 12676 199212 11951 2.72010/08/23 18:53:00 1400 11431 4289 563 1 1 0 2.7 1398 1406 87985 12685 199405 11951 2.82010/08/23 18:54:00 1401 12022 4362 562 1 1 0 2.2 1398 1406 88056 12695 199604 11951 2.82010/08/23 18:55:00 1397 12664 4723 563 1 1 0 2.4 1398 1406 88131 12704 199810 11970 2.82010/08/23 18:56:00 1392 12195 5190 563 1 1 0 2.7 1397 1406 88213 12713 200018 11970 2.72010/08/23 18:57:00 1393 11734 5209 565 1 1 0 2.3 1396 1406 88299 12723 200225 11970 2.72010/08/23 18:58:00 1396 12277 5038 560 1 1 0 2.0 1396 1406 88384 12732 200431 12006 2.72010/08/23 18:59:00 1401 12366 4528 562 1 1 0 2.3 1397 1406 88463 12741 200631 12006 2.62010/08/23 19:00:00 1402 12333 4579 563 1 1 0 2.1 1398 1406 88539 12751 200832 12006 2.62010/08/23 19:01:00 1401 12353 4725 563 1 1 0 1.8 1398 1405 88615 12760 201032 12007 2.62010/08/23 19:02:00 1398 11892 4851 563 1 1 0 2.1 1397 1405 88695 12770 201235 12007 2.52010/08/23 19:03:00 1397 12941 5034 565 1 1 0 2.8 1396 1405 88778 12779 201437 12007 2.52010/08/23 19:04:00 1399 13183 4880 562 1 1 0 2.6 1396 1405 88861 12788 201639 12007 2.52010/08/23 19:05:00 1401 12352 4667 562 1 1 0 2.0 1397 1405 88941 12798 201849 12007 2.52010/08/23 19:06:00 1400 12035 4840 565 1 1 0 1.7 1398 1405 89022 12807 202058 12007 2.42010/08/23 19:07:00 1403 13345 4838 562 1 1 0 1.4 1399 1405 89103 12817 202258 12014 2.32010/08/23 19:08:00 1402 12971 5047 563 1 1 0 1.9 1399 1405 89184 12826 202464 12014 2.3After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/23 19:09:00 1402 12245 4992 568 1 1 0 2.6 1399 1405 89268 12835 202671 12014 2.22010/08/23 19:10:00 1402 13039 5168 565 1 1 0 2.1 1399 1405 89351 12845 202879 12041 2.32010/08/23 19:11:00 1400 12604 5204 562 1 1 0 2.2 1399 1405 89435 12854 203087 12041 2.22010/08/23 19:12:00 1401 12489 5226 565 1 1 0 1.7 1400 1405 89522 12864 203287 12041 2.22010/08/23 19:13:00 1403 11383 5062 562 1 1 0 2.1 1400 1405 89606 12873 203481 12032 2.112032 2.12010/08/23 19:15:00 1402 12765 5015 565 1 1 0 2.7 1400 1405 89773 12892 203881 12032 2.12010/08/23 19:16:00 1403 12338 5061 565 1 1 0 2.5 1400 1405 89857 12901 204084 12046 2.22010/08/23 19:17:00 1410 11008 4385 565 1 1 0 3.0 1401 1405 89935 12911 204279 12046 2.22010/08/23 19:18:00 1409 11784 4346 567 1 1 0 3.2 1402 1405 90006 12920 204467 12046 2.32010/08/23 19:19:00 1399 10739 5177 565 1 1 0 3.1 1402 1405 90084 12930 204659 12065 2.32010/08/23 19:20:00 1393 11718 5709 563 1 1 0 2.4 1402 1405 90175 12939 204844 12065 2.32010/08/23 19:21:00 1396 11163 5515 565 1 1 0 2.6 1401 1405 90269 12948 205032 12065 2.32010/08/23 19:22:00 1402 11520 5185 562 1 1 0 3.6 1401 1405 90358 12958 205221 12086 2.42010/08/23 19:23:00 1408 11191 4733 563 1 1 0 2.9 1402 1405 90439 12967 205417 12086 2.52010/08/23 19:24:00 1408 12151 4579 563 1 1 0 1.9 1402 1405 90515 12977 205609 12086 2.52010/08/23 19:25:00 1407 10997 4682 549 1 1 0 1.3 1403 1405 90591 12986 205799 12087 2.52010/08/23 19:26:00 1408 11177 4381 562 1 1 0 1.6 1403 1405 90667 12995 205987 12087 2.42010/08/23 19:27:00 1405 10888 4688 565 1 1 0 1.7 1404 1405 90743 13005 206175 12087 2.42010/08/23 19:28:00 1398 12317 5142 565 1 1 0 2.5 1404 1405 90825 13014 206362 12094 2.42010/08/23 19:29:00 1399 11076 5320 565 1 1 0 1.9 1403 1405 90915 13023 206553 12094 2.42010/08/23 19:30:00 1403 11016 4985 563 1 1 0 2.4 1403 1405 91001 13033 206741 12094 2.42010/08/23 19:31:00 1404 11760 4999 563 1 1 0 1.5 1403 1405 91085 13042 206936 12116 2.32010/08/23 19:32:00 1402 11173 5130 560 1 1 0 2.2 1403 1405 91169 13052 207131 12116 2.32010/08/23 19:33:00 1405 11004 5047 562 1 1 0 2.1 1402 1405 91255 13061 207325 12116 2.22010/08/23 19:34:00 1412 11660 4317 562 1 1 0 2.5 1402 1405 91333 13070 207517 12120 2.22010/08/23 19:35:00 1411 11647 4411 562 1 1 0 2.3 1403 1405 91405 13080 207708 12120 2.22010/08/23 19:36:00 1395 11497 5483 565 1 1 0 3.2 1404 1405 91486 13089 207896 12120 2.22010/08/23 19:37:00 1382 10431 6693 565 1 1 0 3.0 1403 1404 91588 13099 208081 12121 2.22010/08/23 19:38:00 1389 11329 6337 563 1 1 0 3.4 1402 1404 91697 13108 208272 12121 2.22010/08/23 19:39:00 1400 12723 5631 1910 1 1 0 2.9 1401 1404 91797 13130 208473 12121 2.32010/08/23 19:40:00 1402 11025 5505 2037 1 1 0 2.4 1400 1404 91890 13165 208661 12121 2.32010/08/23 19:41:00 1401 9605 5507 607 1 1 0 2.6 1400 1404 91979 13189 208838 12121 2.42010/08/23 19:42:00 1393 10080 5869 568 1 1 0 3.4 1399 1404 92073 13198 209009 12121 2.52010/08/23 19:43:00 1387 8721 6631 1771 1 1 0 2.6 1398 1404 92180 13218 209163 12089 2.52010/08/23 19:44:00 1392 9601 6349 2460 1 1 0 2.9 1398 1404 92289 13255 209309 12089 2.62010/08/23 19:45:00 1402 8543 5655 2332 1 1 0 2.8 1398 1404 92391 13295 209447 12089 2.62010/08/23 19:46:00 1406 7106 5337 1234 1 1 0 2.6 1398 1404 92483 13327 209580 12006 2.72010/08/23 19:47:00 1407 7763 5257 563 1 1 0 2.8 1398 1404 92572 13339 209710 12006 2.72010/08/23 19:48:00 1400 8185 5590 560 1 1 0 1.9 1398 1404 92662 13348 209838 12006 2.82010/08/23 19:49:00 1392 7041 6297 562 1 1 0 2.3 1397 1404 92763 13358 209965 11947 2.82010/08/23 19:50:00 1396 7885 6208 1666 1 1 0 2.7 1396 1404 92870 13377 210094 11947 2.82010/08/23 19:51:00 1424 7607 4379 1386 1 1 0 2.7 1396 1404 92962 13404 210221 11947 2.82010/08/23 19:52:00 1454 7498 1122 560 1 1 0 3.2 1400 1404 93006 13418 210347 11861 2.82010/08/23 19:53:00 1436 7143 2080 563 1 1 0 2.7 1404 1404 93030 13427 210473 11861 2.72010/08/23 19:54:00 1405 8228 4862 560 1 1 0 2.5 1406 1404 93090 13436 210611 11861 2.72010/08/23 19:55:00 1396 8875 5733 558 1 1 0 2.5 1406 1404 93182 13446 210763 11819 2.72010/08/23After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/23 19:56:00 1402 9815 5314 558 1 1 0 2.0 1406 1404 93275 13455 210923 11819 2.72010/08/23 19:57:00 1411 11542 4623 558 1 1 0 2.2 1406 1404 93358 13464 211100 11819 2.62010/08/23 19:58:00 1414 10609 4165 558 1 1 0 2.2 1408 1404 93431 13474 211286 11799 2.62010/08/23 19:59:00 1411 10796 4425 558 1 1 0 2.6 1410 1404 93501 13483 211475 11799 2.52010/08/23 20:00:00 1406 12333 4884 558 1 1 0 2.4 1410 1404 93578 13492 211676 11799 2.52010/08/23 20:01:00 1402 11938 5054 558 1 1 0 2.2 1410 1404 93660 13502 211879 11817 2.52010/08/23 20:02:00 1407 10852 4691 558 1 1 0 2.3 1410 1404 93743 13511 212081 11817 2.52010/08/23 20:03:00 1424 12323 3257 558 1 1 0 2.0 1411 1404 93810 13520 212283 11817 2.42010/08/23 20:04:00 1423 11775 3063 558 1 1 0 2.3 1413 1404 93860 13530 212488 11831 2.42010/08/23 20:05:00 1409 11981 4083 558 1 1 0 2.0 1415 1404 93918 13539 212692 11831 2.42010/08/23 20:06:00 1399 11857 4853 558 1 1 0 2.2 1414 1404 93993 13548 212897 11831 2.32010/08/23 20:07:00 1396 11573 5327 558 1 1 0 2.0 1411 1404 94079 13557 213098 11837 2.32010/08/23 20:08:00 1397 11819 5327 558 1 1 0 2.1 1408 1404 94169 13567 213297 11837 2.32010/08/23 20:09:00 1406 11845 4667 558 1 1 0 2.1 1407 1404 94253 13576 213496 11837 2.22010/08/23 20:10:00 1411 12421 4050 558 1 1 0 1.7 1407 1404 94325 13585 213706 11842 2.2Run 22010/08/24 07:47:00 1405 11993 4693 478 1 1 0 3 1404 1404 31549 3333 78681 11699 2.92010/08/24 07:48:00 1399 11776 5090 478 1 1 0 3 1404 1404 31630 3341 78876 11699 2.92010/08/24 07:49:00 1399 11493 5260 476 1 1 0 3 1404 1404 31717 3349 79074 11687 2.92010/08/24 07:50:00 1400 11401 5144 476 1 1 0 3 1404 1404 31804 3357 79273 11687 2.92010/08/24 07:51:00 1404 11454 4763 478 1 1 0 3 1403 1404 31887 3365 79467 11687 3.02010/08/24 07:52:00 1405 11747 4682 478 1 1 0 3 1403 1404 31965 3373 79665 11673 3.02010/08/24 07:53:00 1399 11909 5073 480 1 1 0 3 1402 1404 32046 3381 79861 11673 3.02010/08/24 07:54:00 1398 10682 5447 480 1 1 0 3 1402 1404 32136 3389 80054 11673 3.02010/08/24 07:55:00 1407 12646 4766 478 1 1 0 3 1403 1404 32221 3397 80256 11658 3.02010/08/24 07:56:00 1412 11871 4163 478 1 1 0 3 1404 1404 32295 3405 80452 11658 3.02010/08/24 07:57:00 1409 11654 4344 480 1 1 0 3 1404 1404 32364 3413 80652 11658 3.02010/08/24 07:58:00 1401 10739 5185 478 1 1 0 3 1404 1404 32442 3421 80838 11636 3.02010/08/24 07:59:00 1395 12183 5533 478 1 1 0 3 1404 1404 32530 3429 81033 11636 3.02010/08/24 08:00:00 1397 11096 5421 478 1 1 0 3 1403 1404 32623 3437 81224 11636 3.02010/08/24 08:01:00 1403 11904 5078 478 1 1 0 3 1402 1404 32711 3445 81418 11620 3.02010/08/24 08:02:00 1409 11886 4594 476 1 1 0 3 1402 1404 32790 3453 81616 11620 3.02010/08/24 08:03:00 1407 12107 4710 478 1 1 0 3 1403 1404 32868 3461 81813 11620 3.02010/08/24 08:04:00 1407 11664 4631 480 1 1 0 3 1403 1404 32948 3469 82007 11614 3.02010/08/24 08:05:00 1410 11582 4362 480 1 1 0 3 1404 1404 33023 3477 82203 11614 3.02010/08/24 08:06:00 1406 12158 4690 478 1 1 0 3 1405 1404 33097 3485 82401 11614 3.02010/08/24 08:07:00 1399 12533 5248 476 1 1 0 3 1404 1404 33178 3493 82605 11632 3.02010/08/24 08:08:00 1395 11292 5541 478 1 1 0 3 1404 1404 33269 3501 82803 11632 3.02010/08/24 08:09:00 1398 11579 5388 478 1 1 0 3 1404 1404 33361 3509 83000 11632 3.02010/08/24 08:10:00 1404 12098 4986 476 1 1 0 3 1404 1404 33447 3517 83196 11635 3.02010/08/24 08:11:00 1409 12120 4498 478 1 1 0 3 1404 1404 33527 3525 83403 11635 3.02010/08/24 08:12:00 1413 11399 4381 476 1 1 0 3 1404 1404 33601 3532 83598 11635 3.02010/08/24 08:13:00 1412 11980 4122 478 1 1 0 3 1404 1404 33668 3540 83791 11641 3.02010/08/24 08:14:00 1403 11785 4891 478 1 1 0 3 1405 1404 33743 3548 83989 11641 3.12010/08/24 08:15:00 1396 11667 5441 476 1 1 0 3 1405 1404 33829 3556 84189 11641 3.12010/08/24 08:16:00 1396 12094 5730 478 1 1 0 3 1405 1404 33923 3564 84382 11641 3.12010/08/24 08:17:00 1401 11764 5340 476 1 1 0 3 1404 1404 34015 3572 84581 11641 3.1After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 08:18:00 1404 11791 4920 476 1 1 0 3 1404 1404 34101 3580 84779 11641 3.12010/08/24 08:19:00 1407 11918 4781 478 1 1 0 3 1404 1404 34183 3588 84977 11651 3.12010/08/24 08:20:00 1410 11909 4522 476 1 1 0 3 1404 1404 34261 3596 85174 11651 3.12010/08/24 08:21:00 1408 11997 4508 478 1 1 0 4 1404 1404 34335 3604 85370 11651 3.12010/08/24 08:22:00 1399 11836 5280 476 1 1 0 3 1404 1404 34417 3612 85566 11687 3.12010/08/24 08:23:00 1396 11682 5542 476 1 1 0 4 1404 1404 34508 3620 85764 11687 3.12010/08/24 08:24:00 1396 12438 5526 472 1 1 0 3 1404 1404 34601 3628 85953 11687 3.22010/08/24 08:25:00 1398 11195 5525 476 1 1 0 3 1404 1404 34694 3636 86152 11717 3.22010/08/24 08:26:00 1403 11226 5213 476 1 1 0 3 1403 1404 34784 3644 86344 11717 3.22010/08/24 08:27:00 1412 12034 4631 476 1 1 0 3 1403 1404 34865 3652 86538 11717 3.22010/08/24 08:28:00 1411 12319 4362 478 1 1 0 3 1403 1404 34940 3660 86731 11756 3.22010/08/24 08:29:00 1406 11777 4768 480 1 1 0 3 1403 1404 35017 3668 86925 11756 3.22010/08/24 08:30:00 1401 11292 5285 478 1 1 0 3 1403 1404 35102 3676 87116 11756 3.22010/08/24 08:31:00 1399 11529 5421 474 1 1 0 3 1404 1404 35191 3684 87306 11777 3.32010/08/24 08:32:00 1399 11832 5533 478 1 1 0 3 1404 1404 35282 3692 87494 11777 3.32010/08/24 08:33:00 1400 12023 5584 474 1 1 0 3 1404 1404 35374 3700 87689 11777 3.32010/08/24 08:34:00 1403 12247 5231 476 1 1 0 3 1403 1404 35463 3707 87888 11795 3.32010/08/24 08:35:00 1409 11728 4646 478 1 1 0 3 1403 1404 35548 3715 88090 11795 3.32010/08/24 08:36:00 1413 12603 4370 478 1 1 0 3 1403 1404 35622 3723 88278 11795 3.32010/08/24 08:37:00 1409 11323 4684 476 1 1 0 3 1404 1404 35697 3731 88478 11809 3.32010/08/24 08:38:00 1402 11698 5134 478 1 1 0 3 1404 1404 35778 3739 88666 11809 3.32010/08/24 08:39:00 1397 11674 5382 476 1 1 0 3 1404 1404 35866 3747 88855 11809 3.32010/08/24 08:40:00 1396 11949 5745 478 1 1 0 3 1404 1404 35960 3755 89046 11785 3.32010/08/24 08:41:00 1403 11873 5304 478 1 1 0 3 1404 1404 36052 3763 89237 11785 3.32010/08/24 08:42:00 1409 10687 4774 480 1 1 0 3 1404 1404 36135 3771 89430 11785 3.32010/08/24 08:43:00 1418 11469 4053 476 1 1 0 3 1405 1404 36209 3779 89626 11782 3.32010/08/24 08:44:00 1418 12618 3853 478 1 1 0 3 1405 1404 36273 3787 89831 11782 3.32010/08/24 08:45:00 1410 11563 4549 478 1 1 0 3 1406 1404 36343 3795 90028 11782 3.22010/08/24 08:46:00 1402 11562 4938 476 1 1 0 3 1406 1404 36421 3803 90224 11798 3.22010/08/24 08:47:00 1397 11450 5429 476 1 1 0 4 1406 1404 36508 3811 90419 11798 3.32010/08/24 08:48:00 1396 12443 5595 472 1 1 0 4 1406 1404 36600 3819 90620 11798 3.32010/08/24 08:49:00 1398 11384 5405 474 1 1 0 3 1406 1404 36692 3827 90818 11825 3.32010/08/24 08:50:00 1405 12196 4963 474 1 1 0 4 1405 1404 36779 3835 91023 11825 3.32010/08/24 08:51:00 1409 12087 4650 476 1 1 0 4 1405 1404 36859 3842 91220 11825 3.32010/08/24 08:52:00 1421 12249 3551 476 1 1 0 4 1405 1404 36928 3850 91416 11838 3.42010/08/24 08:53:00 1416 10820 3818 478 1 1 0 3 1406 1404 36986 3858 91607 11838 3.42010/08/24 08:54:00 1402 12416 4811 476 1 1 0 3 1407 1404 37058 3866 91794 11838 3.42010/08/24 08:55:00 1396 10840 5390 474 1 1 0 3 1407 1404 37144 3874 92008 11852 3.32010/08/24 08:56:00 1395 11054 5631 478 1 1 0 3 1407 1404 37237 3882 92197 11852 3.32010/08/24 08:57:00 1401 11234 5268 480 1 1 0 3 1406 1404 37328 3890 92387 11852 3.32010/08/24 08:58:00 1409 11660 4621 476 1 1 0 3 1405 1404 37412 3898 92581 11846 3.32010/08/24 08:59:00 1412 11613 4463 478 1 1 0 3 1405 1404 37487 3906 92778 11846 3.32010/08/24 09:00:00 1410 11517 4500 480 1 1 0 3 1405 1404 37560 3914 92971 11846 3.22010/08/24 09:01:00 1416 11485 3984 478 1 1 0 3 1405 1404 37631 3922 93162 11835 32010/08/24 09:02:00 1417 12124 3516 478 1 1 0 3 1406 1404 37691 3930 93354 11835 3.22010/08/24 09:03:00 1402 11703 4707 480 1 1 0 3 1407 1404 37760 3938 93552 11835 3.22010/08/24 09:04:00 1393 12963 5579 476 1 1 0 3 1407 1404 37846 3946 93764 11860 3.2After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 09:05:00 1394 11473 5563 480 1 1 0 3 1407 1404 37939 3954 93966 11860 3.12010/08/24 09:06:00 1402 11545 5102 480 1 1 0 3 1406 1404 38028 3962 94166 11860 3.12010/08/24 09:07:00 1409 11461 4477 480 1 1 0 3 1405 1404 38107 3970 94361 11866 3.02010/08/24 09:08:00 1408 11216 4481 480 1 1 0 3 1405 1404 38181 3978 94558 11866 3.02010/08/24 09:09:00 1407 12015 4640 480 1 1 0 3 1404 1404 38257 3986 94753 11866 3.02010/08/24 09:10:00 1416 11990 3645 480 1 1 0 4 1405 1404 38328 3994 94950 11867 3.02010/08/24 09:11:00 1413 11489 3853 480 1 1 0 3 1407 1404 38389 4002 95142 11867 3.02010/08/24 09:12:00 1403 11477 4634 478 1 1 0 3 1407 1404 38461 4010 95331 11867 3.12010/08/24 09:13:00 1397 11163 5090 478 1 1 0 3 1407 1404 38542 4018 95522 11848 3.12010/08/24 09:14:00 1399 11050 5272 478 1 1 0 3 1406 1404 38630 4026 95713 11848 3.12010/08/24 09:15:00 1407 11524 4686 476 1 1 0 4 1406 1404 38712 4034 95906 11848 3.12010/08/24 09:16:00 1413 12501 4141 480 1 1 0 4 1405 1404 38785 4042 96101 11842 3.12010/08/24 09:17:00 1414 11271 3855 478 1 1 0 3 1405 1404 38850 4050 96294 11842 3.22010/08/24 09:18:00 1408 11476 4178 480 1 1 0 4 1405 1404 38916 4058 96489 11842 3.22010/08/24 09:19:00 1409 11311 4220 478 1 1 0 4 1406 1404 38988 4065 96682 11832 3.22010/08/24 09:20:00 1421 11942 3154 476 1 1 0 4 1407 1404 39049 4073 96877 11832 3.22010/08/24 09:21:00 1418 11329 2948 478 1 1 0 4 1409 1404 39099 4081 97072 11832 3.32010/08/24 09:22:00 1406 11493 4006 480 1 1 0 3 1409 1404 39156 4089 97270 11825 3.32010/08/24 09:23:00 1395 11481 4979 476 1 1 0 3 1409 1404 39233 4097 97467 11825 3.32010/08/24 09:24:00 1399 11888 4785 480 1 1 0 4 1408 1404 39316 4105 97667 11825 3.42010/08/24 09:25:00 1410 12176 3989 478 1 1 0 4 1408 1404 39389 4113 97868 11816 3.42010/08/24 09:26:00 1418 11872 3289 480 1 1 0 3 1407 1404 39450 4121 98070 11816 3.42010/08/24 09:27:00 1415 11714 3202 478 1 1 0 3 1408 1404 39503 4129 98268 11816 3.42010/08/24 09:28:00 1412 11796 3337 478 1 1 0 3 1409 1404 39557 4137 98467 11825 3.42010/08/24 09:29:00 1407 12123 3885 476 1 1 0 4 1410 1404 39618 4145 98665 11825 3.52010/08/24 09:30:00 1420 11912 2822 480 1 1 0 3 1411 1404 39675 4153 98870 11825 3.52010/08/24 09:31:00 1424 11597 2020 480 1 1 0 3 1412 1404 39711 4161 99074 11828 3.52010/08/24 09:32:00 1407 11930 3369 480 1 1 0 3 1412 1404 39753 4169 99282 11828 3.52010/08/24 09:33:00 1390 12006 4765 480 1 1 0 3 1411 1404 39820 4177 99488 11828 3.52010/08/24 09:34:00 1388 12538 5248 482 1 1 0 3 1410 1404 39906 4185 99695 11841 3.42010/08/24 09:35:00 1397 12093 4791 480 1 1 0 3 1408 1404 39989 4193 99902 11841 3.42010/08/24 09:36:00 1410 12443 3637 480 1 1 0 4 1407 1404 40057 4201 100107 11841 3.42010/08/24 09:37:00 1418 12097 2933 482 1 1 0 3 1407 1404 40108 4209 100308 11852 3.42010/08/24 09:38:00 1410 11351 3473 478 1 1 0 3 1408 1404 40160 4217 100506 11852 3.42010/08/24 09:39:00 1402 11829 4228 480 1 1 0 3 1409 1404 40223 4225 100705 11852 3.32010/08/24 09:40:00 1405 12180 3953 480 1 1 0 3 1408 1404 40293 4233 100907 11849 3.32010/08/24 09:41:00 1420 12256 2502 482 1 1 0 4 1408 1404 40344 4241 101108 11849 3.22010/08/24 09:42:00 1417 11716 2416 480 1 1 0 4 1409 1404 40383 4249 101310 11849 3.22010/08/24 09:43:00 1403 11916 3652 480 1 1 0 4 1408 1404 40432 4257 101510 11858 3.22010/08/24 09:44:00 1390 12295 4805 486 1 1 0 4 1407 1404 40504 4265 101711 11858 3.32010/08/24 09:45:00 1392 11981 4748 484 1 1 0 4 1406 1404 40586 4273 101911 11858 3.32010/08/24 09:46:00 1402 11651 4013 484 1 1 0 4 1404 1404 40661 4281 102113 11854 3.32010/08/24 09:47:00 1411 12176 3292 484 1 1 0 4 1403 1404 40722 4289 102316 11854 3.32010/08/24 09:48:00 1415 12171 2680 480 1 1 0 4 1404 1404 40772 4297 102515 11854 3.42010/08/24 09:49:00 1409 12457 3077 484 1 1 0 4 1406 1405 40820 4305 102713 11857 3.42010/08/24 09:50:00 1415 12147 2765 484 1 1 0 4 1407 1405 40873 4313 102924 11857 3.42010/08/24 09:51:00 1407 11920 3297 480 1 1 0 3 1408 1405 40919 4321 103129 11857 3.4After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 09:52:00 1390 12269 4781 480 1 1 0 3 1407 1404 40988 4329 103329 11869 3.32010/08/24 09:53:00 1396 11345 4459 482 1 1 0 3 1405 1404 41068 4338 103525 11869 3.32010/08/24 09:54:00 1405 12029 3781 484 1 1 0 3 1405 1404 41137 4346 103724 11869 3.42010/08/24 09:55:00 1409 11639 3311 484 1 1 0 3 1406 1405 41193 4354 103929 11879 3.42010/08/24 09:56:00 1404 11993 3681 484 1 1 0 3 1405 1405 41250 4362 104129 11879 3.42010/08/24 09:57:00 1399 12259 4141 484 1 1 0 3 1404 1405 41315 4370 104329 11879 3.42010/08/24 09:58:00 1401 11716 4139 480 1 1 0 2 1403 1405 41384 4378 104527 11865 3.32010/08/24 09:59:00 1402 11865 3995 480 1 1 0 3 1404 1405 41451 4386 104727 11865 3.22010/08/24 10:00:00 1407 12067 3776 482 1 1 0 3 1405 1405 41516 4394 104927 11865 3.12010/08/24 10:01:00 1409 12814 3432 484 1 1 0 3 1405 1405 41575 4402 105126 11861 3.12010/08/24 10:02:00 1405 11880 3620 484 1 1 0 4 1405 1405 41634 4410 105325 11861 3.12010/08/24 10:03:00 1405 11678 3642 480 1 1 0 3 1405 1405 41695 4418 105523 11861 3.02010/08/24 10:04:00 1404 12631 3855 484 1 1 0 4 1404 1405 41758 4426 105724 11878 3.02010/08/24 10:05:00 1405 12148 3559 482 1 1 0 4 1404 1405 41821 4434 105922 11878 3.12010/08/24 10:06:00 1406 11989 3654 484 1 1 0 3 1403 1405 41881 4442 106122 11878 3.12010/08/24 10:07:00 1405 12089 3647 484 1 1 0 2 1404 1405 41944 4450 106323 11891 3.12010/08/24 10:08:00 1409 12091 3273 484 1 1 0 2 1405 1405 42001 4458 106524 11891 3.12010/08/24 10:09:00 1411 11643 3063 484 1 1 0 3 1405 1405 42053 4466 106719 11891 3.02010/08/24 10:10:00 1407 11562 3345 484 1 1 0 4 1405 1405 42106 4474 106918 11879 3.12010/08/24 10:11:00 1405 11569 3450 484 1 1 0 4 1405 1405 42162 4483 107116 11879 3.12010/08/24 10:12:00 1401 11536 3827 484 1 1 0 4 1405 1405 42224 4491 107315 11879 3.12010/08/24 10:13:00 1405 12844 3531 486 1 1 0 3 1406 1405 42286 4499 107513 11887 3.22010/08/24 10:14:00 1407 12011 3295 484 1 1 0 4 1406 1405 42342 4507 107719 11887 3.32010/08/24 10:15:00 1405 12053 3508 484 1 1 0 4 1406 1405 42399 4515 107925 11887 3.32010/08/24 10:16:00 1402 12098 3760 486 1 1 0 4 1406 1405 42460 4523 108129 11920 3.42010/08/24 10:17:00 1407 12311 3385 486 1 1 0 4 1406 1405 42520 4531 108333 11920 3.42010/08/24 10:18:00 1403 11711 3834 488 1 1 0 4 1406 1405 42580 4539 108534 11920 3.42010/08/24 10:19:00 1403 12324 3767 484 1 1 0 4 1405 1405 42643 4547 108734 11916 3.42010/08/24 10:20:00 1405 12170 3493 490 1 1 0 3 1405 1405 42703 4555 108936 11916 3.42010/08/24 10:21:00 1405 12243 3652 490 1 1 0 2 1405 1405 42762 4564 109134 11916 3.32010/08/24 10:22:00 1409 11458 3095 492 1 1 0 3 1406 1405 42818 4572 109332 11900 3.32010/08/24 10:23:00 1411 11739 2954 486 1 1 0 2 1406 1405 42867 4580 109531 11900 3.32010/08/24 10:24:00 1408 12132 3054 486 1 1 0 3 1406 1405 42916 4588 109729 11900 3.32010/08/24 10:25:00 1407 12438 3069 484 1 1 0 3 1406 1405 42968 4596 109930 11894 3.32010/08/24 10:26:00 1407 12136 3289 486 1 1 0 3 1406 1405 43021 4604 110133 11894 3.22010/08/24 10:27:00 1402 11897 3513 490 1 1 0 4 1406 1405 43075 4612 110339 11894 3.22010/08/24 10:28:00 1400 12378 3797 488 1 1 0 4 1406 1405 43136 4621 110542 11882 3.22010/08/24 10:29:00 1400 12586 3776 488 1 1 0 3 1405 1405 43200 4629 110742 11882 3.22010/08/24 10:30:00 1405 12174 3478 484 1 1 0 4 1405 1405 43262 4637 110949 11882 3.22010/08/24 10:31:00 1407 12378 3193 492 1 1 0 3 1405 1405 43317 4645 111158 11894 3.22010/08/24 10:32:00 1405 12451 3311 488 1 1 0 3 1405 1405 43372 4653 111362 11894 3.12010/08/24 10:33:00 1402 12059 3387 490 1 1 0 3 1405 1405 43428 4661 111561 11894 3.12010/08/24 10:34:00 1397 11388 4120 494 1 1 0 3 1405 1405 43493 4670 111759 11893 3.12010/08/24 10:35:00 1402 12724 4009 490 1 1 0 4 1405 1405 43560 4678 111965 11893 3.12010/08/24 10:36:00 1408 12035 3452 490 1 1 0 4 1405 1405 43621 4686 112168 11893 3.22010/08/24 10:37:00 1409 12459 3106 494 1 1 0 2 1405 1405 43674 4694 112368 11894 3.22010/08/24 10:38:00 1403 11464 3483 490 1 1 0 2 1404 1405 43729 4702 112564 11894 3.1After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 10:39:00 1399 11988 3778 494 1 1 0 3 1404 1405 43790 4711 112761 11894 3.22010/08/24 10:40:00 1400 12334 3980 488 1 1 0 3 1403 1405 43857 4719 112962 11910 3.22010/08/24 10:41:00 1405 12408 3554 492 1 1 0 2 1403 1405 43919 4727 113161 11910 3.22010/08/24 10:42:00 1407 11602 3276 492 1 1 0 3 1403 1405 43974 4735 113359 11910 3.12010/08/24 10:43:00 1404 12126 3424 494 1 1 0 4 1403 1405 44030 4743 113560 11903 3.12010/08/24 10:44:00 1403 12178 3637 492 1 1 0 4 1404 1405 44090 4752 113758 11903 3.12010/08/24 10:45:00 1404 12664 3618 496 1 1 0 2 1404 1405 44150 4760 113960 11903 3.12010/08/24 10:46:00 1404 11843 3628 496 1 1 0 2 1404 1405 44210 4768 114158 11908 3.02010/08/24 10:47:00 1404 12081 3463 496 1 1 0 4 1404 1405 44270 4776 114360 11908 3.02010/08/24 10:48:00 1403 11424 3618 492 1 1 0 4 1403 1405 44330 4785 114560 11908 3.02010/08/24 10:49:00 1405 11999 3578 492 1 1 0 2 1404 1405 44390 4793 114761 11910 3.02010/08/24 10:50:00 1405 12248 3516 496 1 1 0 2 1404 1405 44451 4801 114963 11910 2.92010/08/24 10:51:00 1402 11868 3748 496 1 1 0 3 1404 1405 44513 4809 115168 11910 2.92010/08/24 10:52:00 1404 12413 3837 496 1 1 0 4 1404 1405 44577 4818 115373 11919 2.92010/08/24 10:53:00 1406 12467 3620 500 1 1 0 4 1403 1405 44638 4826 115580 11919 3.02010/08/24 10:54:00 1406 11542 3457 502 1 1 0 4 1404 1405 44696 4834 115783 11919 3.12010/08/24 10:55:00 1399 12091 3991 502 1 1 0 4 1404 1405 44758 4843 115985 11916 3.22010/08/24 10:56:00 1396 11379 4368 504 1 1 0 4 1403 1405 44828 4851 116188 11916 3.32010/08/24 10:57:00 1401 12368 4009 502 1 1 0 3 1403 1405 44898 4859 116389 11916 3.32010/08/24 10:58:00 1404 11956 3802 502 1 1 0 4 1403 1405 44963 4868 116591 11939 3.42010/08/24 10:59:00 1401 12045 3953 500 1 1 0 4 1403 1405 45027 4876 116794 11939 3.32010/08/24 11:00:00 1399 11873 4148 502 1 1 0 4 1402 1405 45094 4884 116997 11939 3.42010/08/24 11:01:00 1399 11851 4272 504 1 1 0 4 1402 1405 45165 4893 117196 11947 3.52010/08/24 11:02:00 1400 11843 4197 504 1 1 0 3 1402 1405 45236 4901 117396 11947 3.52010/08/24 11:03:00 1401 11905 4356 506 1 1 0 4 1401 1405 45306 4910 117596 11947 3.62010/08/24 11:04:00 1403 11976 3894 504 1 1 0 2 1401 1405 45373 4918 117796 11951 3.52010/08/24 11:05:00 1403 11901 3901 506 1 1 0 2 1401 1405 45440 4926 117993 11951 3.5Run 32010/08/24 11:23:00 1386 11941 5257 504 1 1 0 4 1404 1405 46594 5078 121602 11919 3.12010/08/24 11:24:00 1393 11836 4947 508 1 1 0 3 1403 1405 46681 5086 121802 11919 3.22010/08/24 11:25:00 1403 11345 4297 504 1 1 0 2 1403 1405 46757 5095 121997 11922 3.12010/08/24 11:26:00 1407 11335 3669 508 1 1 0 2 1403 1405 46822 5103 122184 11922 3.12010/08/24 11:27:00 1405 11304 3769 508 1 1 0 4 1403 1405 46884 5112 122379 11922 3.22010/08/24 11:28:00 1405 11607 4024 508 1 1 0 4 1403 1405 46952 5120 122572 11924 3.22010/08/24 11:29:00 1411 11590 3485 508 1 1 0 4 1403 1405 47012 5129 122764 11924 3.22010/08/24 11:30:00 1403 12368 3997 506 1 1 0 4 1403 1405 47076 5137 122960 11924 3.32010/08/24 11:31:00 1401 11793 4512 508 1 1 0 3 1403 1405 47149 5146 123160 11931 3.32010/08/24 11:32:00 1396 11428 4842 508 1 1 0 3 1403 1405 47225 5154 123355 11931 3.32010/08/24 11:33:00 1397 11707 4755 508 1 1 0 3 1402 1405 47306 5162 123547 11931 3.22010/08/24 11:34:00 1402 11920 4487 504 1 1 0 3.3 1401 1405 47385 5171 123743 11918 3.22010/08/24 11:35:00 1405 11465 4087 504 1 1 0 3.9 1400 1405 47458 5179 123936 11918 3.32010/08/24 11:36:00 1407 11603 3926 506 1 1 0 3.9 1400 1405 47526 5188 124128 11918 3.32010/08/24 11:37:00 1406 11703 4004 508 1 1 0 2.4 1401 1404 47594 5196 124319 11908 3.22010/08/24 11:38:00 1415 11759 3163 506 1 1 0 2.4 1402 1404 47654 5205 124507 11908 3.12010/08/24 11:39:00 1408 11591 3679 512 1 1 0 2.2 1404 1404 47710 5213 124701 11908 3.12010/08/24 11:40:00 1402 11629 4173 508 1 1 0 2.4 1404 1405 47775 5222 124895 11922 3.12010/08/24 11:41:00 1399 12013 4483 512 1 1 0 2.2 1404 1405 47847 5230 125092 11922 3.1After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 11:42:00 1399 12711 4508 512 1 1 0 2.9 1403 1405 47922 5239 125285 11922 3.12010/08/24 11:43:00 1396 11732 4794 512 1 1 0 2.7 1403 1404 47999 5247 125480 11923 32010/08/24 11:44:00 1395 12078 5045 508 1 1 0 3 1402 1404 48081 5256 125674 11923 32010/08/24 11:45:00 1402 11454 4453 508 1 1 0 2.8 1402 1404 48160 5264 125868 11923 2.92010/08/24 11:46:00 1405 11807 4295 512 1 1 0 2.8 1402 1404 48231 5273 126057 11909 2.82010/08/24 11:47:00 1410 10952 3832 512 1 1 0 2.8 1403 1404 48298 5281 126248 11909 2.82010/08/24 11:48:00 1410 11434 3478 510 1 1 0 2.5 1404 1404 48358 5290 126439 11909 2.82010/08/24 11:49:00 1405 11590 4173 512 1 1 0 2.4 1404 1405 48422 5298 126627 11897 2.82010/08/24 11:50:00 1398 11885 4714 514 1 1 0 2.5 1404 1405 48495 5307 126818 11897 2.72010/08/24 11:51:00 1396 12045 4974 512 1 1 0 3 1404 1405 48575 5315 127011 11897 2.62010/08/24 11:52:00 1401 11808 4653 512 1 1 0 3.2 1403 1404 48654 5324 127205 11907 2.62010/08/24 11:53:00 1398 11453 4809 512 1 1 0 3.3 1402 1404 48733 5332 127397 11907 2.72010/08/24 11:54:00 1397 11743 5078 512 1 1 0 3 1401 1404 48816 5341 127587 11907 2.72010/08/24 11:55:00 1402 11388 4826 514 1 1 0 2.8 1401 1404 48899 5350 127775 11885 2.82010/08/24 11:56:00 1410 11364 3942 510 1 1 0 2.8 1401 1404 48973 5358 127963 11885 2.82010/08/24 11:57:00 1415 11448 3270 512 1 1 0 3.2 1402 1404 49032 5367 128154 11885 2.82010/08/24 11:58:00 1410 11848 3603 512 1 1 0 2.9 1403 1404 49091 5375 128343 11881 2.82010/08/24 11:59:00 1402 11333 4346 512 1 1 0 2.6 1404 1404 49158 5384 128530 11881 2.82010/08/24 12:00:00 1396 11089 4978 512 1 1 0 2.7 1404 1404 49236 5392 128719 11881 2.82010/08/24 12:01:00 1400 11770 4619 510 1 1 0 4 1403 1404 49318 5401 128912 11890 2.82010/08/24 12:02:00 1403 12158 4522 512 1 1 0 3.7 1403 1404 49394 5409 129104 11890 2.92010/08/24 12:03:00 1404 11703 4309 510 1 1 0 3.3 1403 1404 49467 5418 129294 11890 32010/08/24 12:04:00 1399 11048 4661 510 1 1 0 3.9 1402 1404 49542 5426 129484 11876 3.12010/08/24 12:05:00 1398 11694 4967 512 1 1 0 3.4 1402 1404 49623 5435 129671 11876 3.22010/08/24 12:06:00 1402 12275 4716 512 1 1 0 4.5 1402 1404 49704 5443 129862 11876 3.22010/08/24 12:07:00 1405 10944 4491 510 1 1 0 2.5 1403 1404 49781 5452 130051 11874 3.22010/08/24 12:08:00 1402 10828 4413 512 1 1 0 3.4 1403 1404 49852 5460 130238 11874 3.22010/08/24 12:09:00 1384 11252 5819 518 1 1 0 4.4 1403 1404 49939 5469 130422 11874 3.32010/08/24 12:10:00 1375 11504 6743 520 1 1 0 3.2 1402 1404 50045 5478 130607 11862 3.32010/08/24 12:11:00 1379 10808 6831 3372 1 1 0 2.1 1400 1404 50159 5513 130791 11862 3.32010/08/24 12:12:00 1401 10879 5554 4316 1 1 0 3.3 1398 1404 50264 5579 130974 11862 3.32010/08/24 12:13:00 1470 9161 1663 4495 1 1 0 2 1399 1404 50320 5653 131140 11837 3.32010/08/24 12:14:00 1558 7332 1489 3852 1 1 0 3.3 1407 1404 50344 5726 131276 11837 3.32010/08/24 12:15:00 1611 6658 1184 514 1 1 0 3.8 1419 1404 50364 5752 131395 11837 3.42010/08/24 12:16:00 1597 7547 1184 514 1 1 0 2.7 1433 1407 50382 5761 131516 11770 3.42010/08/24 12:17:00 1555 7287 1074 514 1 1 0 2.1 1445 1407 50400 5769 131634 11770 3.32010/08/24 12:18:00 1501 7537 873 514 1 1 0 2.7 1453 1407 50419 5778 131746 11770 3.22010/08/24 12:19:00 1453 7632 1049 514 1 1 0 2.5 1458 1409 50435 5786 131869 11710 3.12010/08/24 12:20:00 1421 9471 3022 518 1 1 0 2.5 1460 1409 50468 5795 132016 11710 3.12010/08/24 12:21:00 1421 10148 3284 518 1 1 0 2.8 1462 1409 50526 5804 132183 11710 32010/08/24 12:22:00 1481 11554 979 512 1 1 0 3 1465 1409 50555 5812 132363 11693 2.92010/08/24 12:23:00 1484 12175 1032 514 1 1 0 4.1 1470 1409 50573 5821 132566 11693 32010/08/24 12:24:00 1447 11244 873 512 1 1 0 4.1 1475 1409 50590 5829 132761 11693 32010/08/24 12:25:00 1399 10983 4495 518 1 1 0 3.1 1478 1410 50632 5838 132948 11691 32010/08/24 12:26:00 1385 11599 5962 514 1 1 0 3.9 1479 1410 50726 5846 133135 11691 3.12010/08/24 12:27:00 1401 11882 5036 514 1 1 0 3.8 1479 1410 50820 5855 133331 11691 3.22010/08/24 12:28:00 1426 12313 2787 514 1 1 0 3.8 1478 1409 50886 5864 133539 11704 3.2After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 12:29:00 1432 11793 1845 518 1 1 0 4.2 1472 1409 50921 5872 133737 11704 3.32010/08/24 12:30:00 1414 12015 3268 521 1 1 0 3.8 1461 1409 50962 5881 133934 11704 3.32010/08/24 12:31:00 1399 11073 4798 514 1 1 0 4 1448 1409 51030 5889 134122 11694 3.32010/08/24 12:32:00 1395 11049 4958 516 1 1 0 3.5 1436 1409 51113 5898 134307 11694 3.42010/08/24 12:33:00 1400 11421 4604 520 1 1 0 2.3 1427 1409 51193 5907 134496 11694 3.42010/08/24 12:34:00 1405 11614 4266 521 1 1 0 2.4 1422 1409 51267 5915 134687 11671 3.42010/08/24 12:35:00 1409 10164 4015 516 1 1 0 3.3 1420 1409 51335 5924 134868 11671 3.42010/08/24 12:36:00 1408 10766 3795 516 1 1 0 3.9 1420 1409 51402 5932 135046 11671 3.52010/08/24 12:37:00 1403 10808 4293 516 1 1 0 3.1 1417 1409 51469 5941 135229 11649 3.52010/08/24 12:38:00 1400 11675 4655 520 1 1 0 2.2 1411 1409 51545 5950 135417 11649 3.52010/08/24 12:39:00 1400 11024 4644 516 1 1 0 2.7 1407 1409 51622 5958 135609 11649 3.42010/08/24 12:40:00 1403 11195 4487 520 1 1 0 2.4 1405 1409 51698 5967 135798 11642 3.32010/08/24 12:41:00 1405 11106 4348 520 1 1 0 2.7 1406 1409 51771 5976 135984 11642 3.22010/08/24 12:42:00 1403 11081 4324 520 1 1 0 3.4 1407 1409 51843 5984 136171 11642 3.12010/08/24 12:43:00 1401 11294 4475 521 1 1 0 2.3 1406 1409 51919 5993 136358 11617 3.12010/08/24 12:44:00 1402 11460 4557 521 1 1 0 2.2 1404 1409 51996 6002 136547 11617 32010/08/24 12:45:00 1404 10835 4551 521 1 1 0 3.5 1403 1409 52071 6010 136731 11617 2.92010/08/24 12:46:00 1404 10795 4716 520 1 1 0 3.6 1403 1409 52147 6019 136913 11594 2.92010/08/24 12:47:00 1405 11155 4532 520 1 1 0 3.3 1403 1409 52224 6028 137096 11594 2.92010/08/24 12:48:00 1405 11077 4493 520 1 1 0 3.2 1404 1409 52299 6036 137282 11594 2.92010/08/24 12:49:00 1405 10646 4477 521 1 1 0 3 1404 1409 52374 6045 137469 11579 32010/08/24 12:50:00 1403 10776 4536 520 1 1 0 2.7 1403 1409 52449 6054 137653 11579 32010/08/24 12:51:00 1405 11041 4364 520 1 1 0 2.7 1403 1409 52524 6062 137832 11579 2.92010/08/24 12:52:00 1404 10624 4336 520 1 1 0 3.4 1403 1409 52596 6071 138014 11556 2.92010/08/24 12:53:00 1401 10261 4676 520 1 1 0 3.5 1403 1409 52671 6080 138193 11556 2.92010/08/24 12:54:00 1398 11032 4824 521 1 1 0 3.3 1403 1409 52751 6088 138376 11556 32010/08/24 12:55:00 1400 11833 4772 520 1 1 0 2.9 1403 1409 52833 6097 138563 11537 32010/08/24 12:56:00 1405 11109 4580 521 1 1 0 3.1 1403 1409 52910 6106 138753 11537 3.12010/08/24 12:57:00 1406 11020 4324 521 1 1 0 3.4 1403 1409 52983 6114 138944 11537 3.12010/08/24 12:58:00 1405 11397 4344 521 1 1 0 3.1 1403 1409 53056 6123 139133 11521 3.22010/08/24 12:59:00 1403 11714 4469 523 1 1 0 3.1 1403 1409 53130 6132 139323 11521 3.22010/08/24 13:00:00 1402 11195 4619 525 1 1 0 3.1 1403 1409 53206 6140 139515 11521 3.22010/08/24 13:01:00 1401 11050 4691 523 1 1 0 4.1 1403 1409 53284 6149 139704 11512 3.22010/08/24 13:02:00 1402 11700 4686 525 1 1 0 4 1403 1409 53361 6158 139893 11512 3.22010/08/24 13:03:00 1405 11020 4526 525 1 1 0 3.6 1403 1409 53438 6167 140079 11512 3.32010/08/24 13:04:00 1409 10913 4124 527 1 1 0 3.4 1403 1409 53509 6175 140267 11495 3.32010/08/24 13:05:00 1411 11202 4020 527 1 1 0 2.8 1404 1409 53574 6184 140456 11495 3.32010/08/24 13:06:00 1401 11432 4678 523 1 1 0 2.1 1404 1409 53646 6193 140646 11495 3.32010/08/24 13:07:00 1393 11567 5277 525 1 1 0 3 1403 1409 53729 6202 140834 11478 3.32010/08/24 13:08:00 1395 10952 5240 529 1 1 0 2.5 1403 1409 53818 6210 141025 11478 3.22010/08/24 13:09:00 1403 11205 4802 525 1 1 0 3.4 1403 1409 53902 6219 141213 11478 3.12010/08/24 13:10:00 1407 11619 4317 525 1 1 0 2.9 1403 1409 53976 6228 141403 11477 3.12010/08/24 13:11:00 1407 11517 4094 525 1 1 0 3 1404 1409 54047 6237 141595 11477 3.12010/08/24 13:12:00 1403 10996 4528 527 1 1 0 3.7 1403 1409 54121 6245 141784 11477 3.12010/08/24 13:13:00 1406 11403 4524 525 1 1 0 3.1 1403 1409 54198 6254 141971 11466 3.12010/08/24 13:14:00 1406 11220 4534 525 1 1 0 3 1403 1409 54274 6263 142160 11466 3.12010/08/24 13:15:00 1404 11605 4746 523 1 1 0 3.2 1403 1409 54350 6272 142348 11466 3.1After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 13:16:00 1399 11052 5102 527 1 1 0 2.5 1403 1409 54429 6280 142535 11438 3.12010/08/24 13:17:00 1395 10955 5431 527 1 1 0 3.2 1403 1409 54517 6289 142721 11438 32010/08/24 13:18:00 1400 11861 5102 527 1 1 0 3 1402 1409 54607 6298 142909 11438 32010/08/24 13:19:00 1406 11664 4536 527 1 1 0 3 1402 1409 54687 6307 143100 11428 32010/08/24 13:20:00 1409 11193 4278 529 1 1 0 4.4 1402 1409 54760 6315 143288 11428 2.92010/08/24 13:21:00 1412 10488 3871 525 1 1 0 3.3 1402 1409 54828 6324 143471 11428 3.12010/08/24 13:22:00 1405 11550 4485 525 1 1 0 3 1403 1409 54897 6333 143653 11412 3.12010/08/24 13:23:00 1399 12119 4992 523 1 1 0 2.7 1404 1409 54975 6342 143844 11412 3.12010/08/24 13:24:00 1399 11449 4929 521 1 1 0 2.9 1404 1409 55058 6350 144035 11412 3.12010/08/24 13:25:00 1402 11563 4860 521 1 1 0 3 1403 1409 55141 6359 144226 11417 3.12010/08/24 13:26:00 1403 11599 4908 525 1 1 0 3.1 1403 1409 55221 6368 144416 11417 3.22010/08/24 13:27:00 1401 11760 4967 525 1 1 0 2.4 1403 1409 55304 6377 144608 11417 3.12010/08/24 13:28:00 1403 10985 4789 523 1 1 0 3.4 1403 1409 55384 6385 144798 11396 3.12010/08/24 13:29:00 1407 11303 4493 525 1 1 0 3.3 1403 1409 55461 6394 144986 11396 3.12010/08/24 13:30:00 1413 11879 3781 525 1 1 0 2.7 1403 1409 55530 6403 145176 11396 3.12010/08/24 13:31:00 1409 12014 4143 525 1 1 0 4.3 1404 1409 55596 6412 145365 11386 3.22010/08/24 13:32:00 1402 11773 4701 521 1 1 0 3.9 1405 1409 55669 6420 145557 11386 3.32010/08/24 13:33:00 1400 11799 4846 525 1 1 0 3 1405 1409 55748 6429 145752 11386 3.32010/08/24 13:34:00 1400 11645 4835 520 1 1 0 2.5 1405 1409 55829 6438 145945 11383 3.22010/08/24 13:35:00 1398 12067 5135 529 1 1 0 2.8 1404 1409 55912 6446 146139 11383 3.22010/08/24 13:36:00 1402 11724 4789 525 1 1 0 3 1404 1409 55995 6455 146339 11383 3.12010/08/24 13:37:00 1408 12134 4319 523 1 1 0 2.3 1403 1409 56072 6464 146538 11381 3.12010/08/24 13:38:00 1412 11508 3955 525 1 1 0 2.5 1404 1409 56141 6473 146732 11381 3.12010/08/24 13:39:00 1414 12232 3814 525 1 1 0 2.7 1405 1409 56206 6481 146925 11381 3.12010/08/24 13:40:00 1406 12397 4305 525 1 1 0 2.3 1405 1409 56272 6490 147120 11370 32010/08/24 13:41:00 1400 12457 4824 521 1 1 0 2.6 1406 1409 56349 6499 147318 11370 32010/08/24 13:42:00 1401 11667 4849 518 1 1 0 2.8 1405 1409 56430 6508 147518 11370 32010/08/24 13:43:00 1402 12300 4705 525 1 1 0 3 1405 1409 56507 6516 147712 11368 32010/08/24 13:44:00 1398 12027 4979 521 1 1 0 3.1 1405 1409 56587 6525 147906 11368 2.92010/08/24 13:45:00 1399 11788 4995 525 1 1 0 3.5 1404 1409 56670 6534 148104 11368 2.92010/08/24 13:46:00 1402 11551 4716 525 1 1 0 3.5 1404 1409 56752 6542 148298 11362 2.92010/08/24 13:47:00 1409 12311 4226 525 1 1 0 3.8 1403 1409 56827 6551 148492 11362 2.92010/08/24 13:48:00 1415 11307 3695 525 1 1 0 3.9 1404 1409 56892 6560 148685 11362 2.92010/08/24 13:49:00 1409 11664 3928 527 1 1 0 2.9 1405 1409 56952 6569 148877 11354 32010/08/24 13:50:00 1403 12345 4481 521 1 1 0 3 1406 1409 57022 6577 149075 11354 32010/08/24 13:51:00 1399 12487 4851 527 1 1 0 2.7 1406 1409 57100 6586 149272 11354 32010/08/24 13:52:00 1400 11356 4826 527 1 1 0 3.3 1405 1409 57180 6595 149468 11345 32010/08/24 13:53:00 1398 11995 4911 527 1 1 0 3.8 1404 1409 57262 6604 149668 11345 3.12010/08/24 13:54:00 1399 11848 4994 529 1 1 0 4.4 1403 1409 57345 6613 149869 11345 3.22010/08/24 13:55:00 1405 12184 4441 529 1 1 0 3.4 1403 1409 57425 6622 150068 11350 3.32010/08/24 13:56:00 1409 11739 4131 529 1 1 0 3.4 1403 1409 57497 6630 150265 11350 3.42010/08/24 13:57:00 1415 11754 3640 529 1 1 0 2.6 1404 1409 57562 6639 150460 11350 3.42010/08/24 13:58:00 1412 11514 3695 529 1 1 0 2.5 1405 1409 57619 6648 150656 11357 3.42010/08/24 13:59:00 1405 12017 4190 529 1 1 0 2.3 1406 1409 57684 6657 150852 11357 3.32010/08/24 14:00:00 1401 11331 4559 529 1 1 0 3.2 1406 1409 57758 6666 151050 11357 3.32010/08/24 14:01:00 1402 11432 4508 529 1 1 0 3.2 1406 1409 57834 6674 151247 11351 3.32010/08/24 14:02:00 1401 11767 4493 533 1 1 0 4 1406 1409 57910 6683 151443 11351 3.2After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 14:03:00 1398 12987 4820 529 1 1 0 3.7 1405 1409 57988 6692 151641 11351 3.32010/08/24 14:04:00 1400 11688 4824 533 1 1 0 3.3 1404 1409 58069 6701 151839 11352 3.32010/08/24 14:05:00 1402 11909 4659 531 1 1 0 2.6 1403 1409 58147 6710 152038 11352 3.32010/08/24 14:06:00 1409 11645 4107 531 1 1 0 2.8 1404 1409 58222 6719 152235 11352 3.32010/08/24 14:07:00 1422 12098 3005 533 1 1 0 2.5 1405 1409 58280 6727 152433 11348 3.22010/08/24 14:08:00 1413 11581 3297 529 1 1 0 2.3 1406 1409 58330 6736 152628 11348 3.22010/08/24 14:09:00 1401 11881 4360 529 1 1 0 2.3 1407 1409 58394 6745 152829 11348 3.12010/08/24 14:10:00 1399 11764 4688 529 1 1 0 2.9 1406 1409 58471 6754 153029 11353 32010/08/24 14:11:00 1401 11773 4489 533 1 1 0 3.1 1406 1409 58547 6763 153224 11353 2.92010/08/24 14:12:00 1399 12327 4634 529 1 1 0 3.1 1405 1409 58623 6772 153423 11353 2.92010/08/24 14:13:00 1397 12180 4820 529 1 1 0 2.6 1404 1409 58703 6781 153630 11369 32010/08/24 14:14:00 1400 11166 4663 533 1 1 0 2.7 1403 1409 58783 6789 153829 11369 32010/08/24 14:15:00 1403 11450 4506 527 1 1 0 2.8 1403 1409 58860 6798 154025 11369 32010/08/24 14:16:00 1407 11291 4152 529 1 1 0 3.2 1403 1409 58934 6807 154217 11367 32010/08/24 14:17:00 1414 11595 3475 531 1 1 0 2.9 1404 1409 58996 6816 154410 11367 32010/08/24 14:18:00 1412 11619 3483 527 1 1 0 3.2 1405 1409 59054 6825 154605 11367 2.92010/08/24 14:19:00 1396 12279 4632 531 1 1 0 3.2 1405 1409 59119 6834 154803 11356 2.92010/08/24 14:20:00 1385 12018 5846 533 1 1 0 3.4 1405 1409 59210 6842 155003 11356 2.92010/08/24 14:21:00 1393 11756 5396 533 1 1 0 3.5 1403 1409 59306 6851 155202 11356 32010/08/24 14:22:00 1409 11185 4079 533 1 1 0 3.5 1402 1409 59385 6860 155395 11348 32010/08/24 14:23:00 1417 11016 3273 533 1 1 0 3.3 1402 1409 59445 6869 155584 11348 3.12010/08/24 14:24:00 1409 10215 3874 533 1 1 0 4 1403 1409 59502 6878 155762 11348 3.22010/08/24 14:25:00 1400 10295 4671 533 1 1 0 4.6 1403 1409 59574 6887 155934 11312 3.32010/08/24 14:26:00 1396 10834 4986 533 1 1 0 4.4 1403 1409 59655 6896 156112 11312 3.32010/08/24 14:27:00 1395 11252 5146 533 1 1 0 3.3 1402 1409 59740 6905 156304 11312 3.42010/08/24 14:28:00 1397 11361 5099 533 1 1 0 2.3 1402 1409 59825 6913 156496 11313 3.42010/08/24 14:29:00 1403 11331 4632 533 1 1 0 2.6 1403 1409 59906 6922 156689 11313 3.42010/08/24 14:30:00 1406 11094 4350 533 1 1 0 3.6 1403 1409 59979 6931 156880 11313 3.42010/08/24 14:31:00 1407 11333 4362 533 1 1 0 2.9 1403 1409 60052 6940 157071 11303 3.42010/08/24 14:32:00 1413 12082 3729 531 1 1 0 3.2 1403 1409 60118 6949 157261 11303 3.42010/08/24 14:33:00 1413 11909 3442 533 1 1 0 3.4 1403 1409 60177 6958 157455 11303 3.42010/08/24 14:34:00 1406 11494 4342 535 1 1 0 3.8 1403 1410 60242 6967 157652 11305 3.42010/08/24 14:35:00 1400 11688 4716 533 1 1 0 3.6 1404 1410 60317 6976 157849 11305 3.42010/08/24 14:36:00 1401 11815 4496 533 1 1 0 3 1405 1410 60394 6984 158044 11305 3.42010/08/24 14:37:00 1397 11427 4986 533 1 1 0 3.3 1405 1410 60472 6993 158242 11313 3.42010/08/24 14:38:00 1397 11751 4938 533 1 1 0 4.1 1404 1410 60555 7002 158443 11313 3.42010/08/24 14:39:00 1405 11852 4553 536 1 1 0 4.3 1403 1410 60635 7011 158644 11313 3.42010/08/24 14:40:00 1409 11436 3982 538 1 1 0 3.2 1403 1410 60704 7020 158836 11308 3.42010/08/24 14:41:00 1411 11224 3818 538 1 1 0 4.2 1404 1410 60770 7029 159029 11308 3.42010/08/24 14:42:00 1414 11230 3319 535 1 1 0 2.7 1405 1410 60829 7038 159222 11308 3.42010/08/24 14:43:00 1407 11922 3767 535 1 1 0 1.9 1406 1410 60889 7047 159420 11318 3.42010/08/24 14:44:00 1401 11994 4528 542 1 1 0 2.9 1406 1410 60959 7056 159618 11318 3.32010/08/24 14:45:00 1399 11783 4665 538 1 1 0 2.8 1406 1410 61036 7065 159819 11318 3.42010/08/24 14:46:00 1396 11893 4974 535 1 1 0 2.4 1405 1410 61115 7074 160014 11322 3.32010/08/24 14:47:00 1394 12325 5090 536 1 1 0 2.7 1404 1410 61199 7083 160213 11322 3.32010/08/24 14:48:00 1399 11772 4829 536 1 1 0 3.2 1403 1410 61283 7092 160412 11322 3.32010/08/24 14:49:00 1407 11218 4375 538 1 1 0 3 1403 1410 61360 7101 160609 11315 3.2After BurnTempWeighbeltFlowOxidizer GasFlowDryer GasFlowWeighbeltONDryer GasFlowWeighbeltErrorBaghousedPOxidizer15m avgOxidizer3Hr avgOxid DayTotalDryer DayTotalWtBelt DayTotalWtBelt 3HravgBaghouse15m avgDate Time °F LB/HR SCFH SCFH in.wc degF degF SCF SCF LBS LBS/HR2010/08/24 14:50:00 1416 11206 3633 538 1 1 0 3.1 1403 1410 61428 7110 160798 11315 3.22010/08/24 14:51:00 1416 10899 3356 540 1 1 0 3.7 1404 1410 61485 7119 160985 11315 3.22010/08/24 14:52:00 1406 11296 4182 535 1 1 0 3.9 1405 1410 61547 7128 161170 11305 3.22010/08/24 14:53:00 1399 11594 4708 538 1 1 0 3.7 1405 1410 61622 7137 161362 11305 3.22010/08/24 14:54:00 1400 11356 4815 538 1 1 0 3.7 1405 1410 61703 7146 161556 11305 3.22010/08/24 14:55:00 1404 11287 4657 540 1 1 0 3.7 1404 1410 61780 7155 161748 11316 3.22010/08/24 14:56:00 1399 11982 4676 540 1 1 0 3.5 1404 1410 61856 7163 161942 11316 3.22010/08/24 14:57:00 1399 11453 4811 538 1 1 0 3.5 1403 1410 61937 7173 162135 11316 3.22010/08/24 14:58:00 1404 10993 4536 544 1 1 0 4 1402 1410 62015 7182 162326 11330 3.32010/08/24 14:59:00 1407 11429 4154 540 1 1 0 4.1 1402 1410 62086 7191 162512 11330 3.42010/08/24 15:00:00 1416 11427 3286 540 1 1 0 3.9 1403 1410 62149 7200 162698 11330 3.52010/08/24 15:01:00 1414 10812 3313 540 1 1 0 3.7 1405 1410 62202 7209 162889 11316 3.62010/08/24 15:02:00 1405 11280 4009 540 1 1 0 3.5 1405 1410 62263 7218 163081 11316 3.62010/08/24 15:03:00 1401 12054 4411 542 1 1 0 3.2 1406 1410 62335 7227 163275 11316 3.72010/08/24 15:04:00 1400 12033 4536 540 1 1 0 4 1406 1410 62410 7236 163468 11314 3.72010/08/24 15:05:00 1398 11272 4857 540 1 1 0 4 1405 1410 62487 7245 163662 11314 3.72010/08/24 15:06:00 1397 12108 5006 540 1 1 0 3.4 1404 1410 62570 7254 163859 11314 3.82010/08/24 15:07:00 1404 12251 4481 545 1 1 0 2.4 1403 1410 62650 7263 164056 11326 3.72010/08/24 15:08:00 1409 11558 4004 540 1 1 0 2.8 1403 1410 62720 7272 164244 11326 3.6

# Appendix G Agency Communications

# Appendix H USEPA ICR Reporting TablesParameterSample 1 Sample 2 Sample 3 Unit of MeasureOtherSupportingInformationDate of Testing8/23/2010 8/24/2010 8/24/2010Feed/Charge Rate5.37 5.39 5.15Mg/hrAfterburner Operating Temperature1405 1405 1409degree FAverageType of Charge: Aluminum ChipsCompoundVolatile Organic HAPEmission Rate Sample 1(kg/hr)Volatile Organic HAPEmission Rate Sample 1(kg/Mg of feed/charge)Volatile Organic HAPEmission Rate Sample2 (kg/hr)VolatileOrganicHAPEmission RateSample 2 (kg/Mg offeed/charge)Volatile Organic HAPEmission Rate Sample 3(kg/hr)VolatileOrganicHAPEmission RateSample 3 (kg/Mg offeed/charge)Test MethodUsedDetection LimitInformation(BDL,DLL,ADL)Other SupportingInformationAcrylonitrile 107-13-14.44661E‐05 8.27322E‐06 4.47445E‐05 8.30679E‐06 4.30241E‐05 8.3495E‐06 Method0031 BDLBenzene 71-43-25.18052E‐06 9.6387E‐07 5.03239E‐06 9.34261E‐07 4.8389E‐06 9.39064E‐07 Method0031 BDLBromodichloromethane 75-27-43.88539E‐06 7.22902E‐07 3.829E‐06 7.1085E‐07 3.68177E‐06 7.14505E‐07 Method0031 BDLCarbon disulfide 75-15-08.60182E‐05 1.60043E‐05 3.282E‐05 6.093E‐06 1.56738E‐05 3.04175E‐06 Method0031 DLLCarbon tetrachloride 56-23-57.07464E‐05 1.31628E‐05 2.2602E‐05 4.19605E‐06 3.25889E‐05 6.32439E‐06 Method0031 BDLChlorodibromomethane 124-48-16.25979E‐06 1.16468E‐06 4.48539E‐06 8.3271E‐07 5.47006E‐06 1.06155E‐06 Method0031 DLLChloroform 67-66-33.75587E‐06 6.98806E‐07 3.73054E‐06 6.92571E‐07 3.5871E‐06 6.96132E‐07 Method0031 BDLChloroprene 126-99-88.6342E‐06 1.60645E‐06 8.75199E‐06 1.6248E‐06 8.41548E‐06 1.63315E‐06 Method0031 BDLDibromomethane 74-95-36.6915E‐06 1.245E‐06 6.23579E‐06 1.15767E‐06 5.68045E‐06 1.10238E‐06 Method0031 BDL1,1-Dichloroethane 75-34-33.88539E‐06 7.22902E‐07 3.829E‐06 7.1085E‐07 3.68177E‐06 7.14505E‐07 Method0031 BDL1,2-Dichloroethane 107-06-24.74881E‐06 8.83547E‐07 4.70419E‐06 8.7333E‐07 4.52332E‐06 8.77821E‐07 Method0031 BDL1,1-Dichloroethene 75-35-49.92932E‐06 1.84742E‐06 9.73659E‐06 1.80759E‐06 9.36222E‐06 1.81688E‐06 Method0031 BDLtrans-1,2-Dichloroethene 156-60-51.80239E‐05 3.35346E‐06 1.45502E‐05 2.70123E‐06 1.33596E‐05 2.59263E‐06 Method0031 BDL1,2-Dichloropropane 78-87-54.96466E‐06 9.23709E‐07 4.70419E‐06 8.7333E‐07 4.52332E‐06 8.77821E‐07 Method0031 BDL1,3-Dichloropropene 542-75-69.79981E‐06 1.82332E‐06 9.75847E‐06 1.81165E‐06 9.19391E‐06 1.78422E‐06 Method0031 BDLLabanalysisincludesthecis‐andtrans‐isomersseparately.ResultshavebeencombinedforthisworksheetMethylene chloride 75-09-20.000863851 0.000160725 0.000831767 0.000154417 0.000715631 0.000138879 Method0031 DLLTetrachloroethene 127-18-41.41385E‐05 2.63056E‐06 8.75199E‐06 1.6248E‐06 9.15183E‐06 1.77606E‐06 Method0031 BDLToluene 108-88-39.92932E‐06 1.84742E‐06 1.55348E‐05 2.88402E‐06 1.45167E‐05 2.81719E‐06 Method0031 BDL1,1,1-Trichloroethane 71-55-65.18052E‐06 9.6387E‐07 5.03239E‐06 9.34261E‐07 4.8389E‐06 9.39064E‐07 Method0031 BDL1,1,2-Trichloroethane 79-00-54.74881E‐06 8.83547E‐07 4.70419E‐06 8.7333E‐07 4.52332E‐06 8.77821E‐07 Method0031 BDLTrichloroethene 79-01-64.74881E‐06 8.83547E‐07 4.70419E‐06 8.7333E‐07 4.52332E‐06 8.77821E‐07 Method0031 BDLTrichlorofluoromethane 75-69-41.77001E‐05 3.29322E‐06 1.78322E‐05 3.31053E‐06 1.71465E‐05 3.32755E‐06 Method0031 BDLMiscellaneous Organics8.6342E‐07 1.60645E‐07 7.65799E‐07 1.4217E‐07 7.36354E‐07 1.42901E‐07 Method0031 BDLSpeciated Volatile Organic HAP Emission Data (Method 0031)Facility Name and Address Unit Description Process Unit IDControl Device IDGeneralMotorsLLC105GMDrive,Bedford,IN47421NaturalGas‐FiredAluminumThermalChipDryerCHIP‐2 AB‐1ParameterSample 1 Sample 2 Sample 3 Unit of MeasureOtherSupportingInformationDate of Testing8/23/2010 8/24/2010 8/24/2010Feed/Charge Rate5.38 5.39 5.15Mg/hrAfterburner Operating Temperature1405 1405 1409degree FAverageType of Charge: Aluminum ChipsCompoundSemi-volatile Organic HAPEmission Rate Sample 1(kg/hr)Semi-volatile Organic HAPEmission Rate Sample 1(kg/Mg of feed/charge)Semi-volatile OrganicHAP Emission RateSample 2 (kg/hr)Semi-volatile Organic HAPEmission Rate Sample 2(kg/Mg of feed/charge)Semi-volatile OrganicHAP Emission RateSample 3 (kg/hr)Semi-volatileOrganicHAP Emission RateSample 3 (kg/Mg offeed/charge) Test Method UsedDetection LimitInformation(BDL,DLL,ADL)1Other SupportingInformationAcenaphthene 83-32-91.77803E‐063.30786E‐074.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(ADL,BDL,BDL)Acenaphthylene 208-96-84.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(ADL,BDL,BDL)Anthracene 120-12-71.48169E‐062.75655E‐074.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(ADL,BDL,BDL)Benz[a]anthracene 56-55-34.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(BDL,BDL,BDL)Benzo[a]pyrene 50-32-84.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(BDL,BDL,BDL)Benzo[b]fluoranthene 205-99-24.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(BDL,BDL,BDL)Benzo[g,h,i]perylene 191-24-24.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(BDL,BDL,BDL)Benzo[k]fluoranthene 207-08-94.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(BDL,BDL,BDL)Chrysene 218-01-94.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(BDL,BDL,BDL)Dibenz[a,h]anthracene 53-70-34.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(BDL,BDL,BDL)Fluoranthene 206-44-01.87681E‐063.49163E‐071.11902E‐062.07711E‐074.90264E‐079.52273E‐08Method0010(ADL,ADL,BDL)Fluorene 86-73-78.39625E‐061.56205E‐061.02172E‐061.89649E‐074.90264E‐079.52273E‐08Method0010(ADL,ADL,BDL)Indeno(1,2,3-cd)pyrene 193-39-54.93897E‐079.18851E‐084.86532E‐079.03092E‐084.90264E‐079.52273E‐08Method0010(BDL,BDL,BDL)Naphthalene 91-20-39.1371E‐05 1.69987E‐051.51798E‐052.81765E‐063.54951E‐056.89445E‐06Method0010(ADL,ADL,ADL)Phenanthrene 85-01-82.16821E‐054.03376E‐063.16246E‐065.8701E‐072.15716E‐064.19E‐07 Method0010(ADL,ADL,ADL)Pyrene 129-00-04.93897E‐079.18851E‐081.50825E‐062.79959E‐074.90264E‐079.52273E‐08Method0010(BDL,ADL,BDL)1. Acronyms are listed in order corresponding to Samples 1-3.Speciated Volatile Organic HAP Emission Data (Method 0010)Facility Name and Address Unit IDUnit Type (Chip dryer or scrapdryer /delacq /decoating kiln)GeneralMotorsLLC105GMDrive,Bedford,IN47421CHIP‐2NaturalGas‐FiredAluminumThermalChipDryerParameterSample 1 Sample 2 Sample 3 Unit of MeasureOther SupportingInformationDate of Testing8/23/2010 8/24/2010 8/24/2010Feed/Charge Rate5.38 5.39 5.15Mg/hrAfterburner residence timeUnkown Unkown UnkownsecAfterburner Operating Temperature1405 1405 1409degree FAverage1 8/23/2010 16:49 8/23/2010 20:102 8/24/2010 7:47 8/24/2010 10:563 8/24/2010 11:52 8/24/2010 15:06Run Number THC Emission Rate (kg/hr)THC Emission Rate (kg/Mgof feed/charge)Data Flag (ADL, BDL, DDL)***Detection Limit(ng/dscm)1 0.667 0.124 ADLUsedonlineanalyzertogetppmreadingonwetbasis.2 0.631 0.117 ADLUsedonlineanalyzertogetppmreadingonwetbasis.3 0.122 0.024 ADLUsedonlineanalyzertogetppmreadingonwetbasis.*** See Appendix A to Enclosure 1Test End TimeRun Number Test Start Date Test Start Time Test End DateFacility Name and Address Unit Description Process Unit IDControl Device IDGeneralMotorsLLC105GMDrive,Bedford,IN47421NaturalGas‐FiredAluminumThermalChipDryerCHIP‐2 AB‐1ParameterSample 1 Sample 2 Sample 3 Unit of MeasureOtherSupportingInformationDate of Testing8/23/2010 8/24/2010 8/24/2010Feed/Charge Rate5.38 5.39 5.15Mg/hrAfterburner Operating Temperature1405 1405 1409degree FAverageFlow Rate663.2 654.9 646.6actualM3/minFlow Rate364.7 363.5 365.0drysM3/minEmission Test Results ConstituentCompositionSample 1(%)CompositionSample 2(%)CompositionSample 3(%)Test Method Used(ex. U.S. EPA Method 3B) Other Supporting InformationO216.2 16.2 16.6 3ACO22.5 3.1 2.4 3AH2O18.87 20.61 19.89 4MoisturesfromMethod0031traingiveresultsof(0.59%,0.67%,and0.64%)whicharenotaccurate.ResultsreportedherearefromMethod0010sampingtrain.Facility Name and Address Unit Description Process Unit IDControl Device ID*GeneralMotorsLLC105GMDrive,Bedford,IN47421NaturalGas‐FiredAluminumThermalChipDryerCHIP‐2 AB‐1(Baghouse)Sample ID No.____CHIP BH DUST COMP 1 - 3_________________Type of Sample (Lime or Particulate):____Particulate_______________Date SampledDate(s)Analyzed8/25/20109/2/10and9/3/10HAP Metalmg/kg mg/kg mg/kg Average(mg/kg)Antimony<20.0 <20.0 <20.0 <20.0Beryllium<0.967 <0.915 <0.949 <0.944Chromium643 446 556 548Hexavalent chromium<10.0 <10.0 <10.0 <10.0Lead4710 3260 3990 3987Mercury<0.05 <0.05 <0.05 <0.05Selenium<20.0 <20.0 <20.0 <20.0Arsenic1370 959 1240 1190Cadmium42.1 29.5 36.9 36Cobalt34.1 24.5 30.3 30Manganese4030 2730 3420 3393Nickel506 354 443 434* Enter multiple control device ID Nos. if the lime results apply to mulitiple control devices.