U.S. EPA Data Request 

Emissions Test Report 

Prepared for: 

Johns Manville 

McPherson Plant 

1465 17th Avenue 

McPherson, Kansas 67460 

Project No. 11-4191.03 

February 22, 2012 

BT Environmental Consulting, Inc. 

4949 Fernlee Avenue 

Royal Oak, Michigan 48073 

(248) 548-8070 
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

i

Executive Summary 

For the purpose of assisting in the development of any emission standard under Section 7412 of 

the Clean Air Act (CAA), Section 114 of the CAA gives the United States Environmental 

Protection Agency (U.S. EPA) authority to require that persons who operate any emission source 

“sample such emissions (in accordance with such procedures or methods, at such locations, at 

such intervals, during such periods and in such manner as the Administrator shall prescribe)”. 

Consistent with this authority, U.S. EPA has required that Johns Manville (JM) sample emissions 

for the purpose of providing residual risk-related data for the National Emission Standards for 

Hazardous Air Pollutants (NESHAP) for Wool Fiberglass Manufacturing1. 

To assist in collecting the agreed upon data, BT Environmental Consulting, Inc. (BTEC) was 

retained by JM to evaluate emission rates of the following pollutants from three exhaust stacks 

associated with the Line 122 Melter Dust Collector (2 stacks) and the Line 123 Melter Dust 

Collector (1 stack) located at the Johns Manville plant in McPherson, Kansas: 

• Filterable particulate matter (PM) using U.S. EPA Methods 5/29 

• Filterable chromium (FCr) using U.S. EPA Method 29 

• Vaporous chromium (VCr) using U.S. EPA Method 29 

• Total chromium (TCr) using U.S. EPA Method 29 

• Hexavalent chromium (Cr+6) using SW-846 Method 0061 

• TCr using SW-846 Method 0061 

Tables I, and II on the following pages summarize the overall results of the emissions test 

program. 

 

1

 Codified at 40 CFR 63, Subpart NNN 
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

ii

Table I 

Overall Emissions Test Results Summary 

Line 122 Melter Dust Collector North and South 

Test Dates: February 1 and 2, 2012 

Test Methods Pollutant MDL 

used 

Emission 

Rate 

(lbs/hour) 

Emission 

Rate 

(lbs/ton) 

Emission 

Rate 

(mg/dscm) 

USEPA 

Method 5/29 Filterable PM < 1.5 x 10-1 9.5 x 10-1 

USEPA 

Method 29 

Filterable Chromium 

(FCr) < 1.3 x 10-4 8.8 x 10-4

Vaporous Chromium 

(VCr) < 5.6 x 10-6 3.5 x 10-5

Total Chromium (TCr) < 1.4 x 10-4 9.2 x 10-4

USEPA 

Method 0061 

Hexavalent Chromium 

(Cr+6) < 1.1 x 10-5 6.9 x 10-5

Total Chromium (TCr) < 1.8 x 10-4 1.2 x 10-3

Table II 

Overall Emissions Test Results Summary 

Line 123 Melter Dust Collector 

Test Dates: January 30 and 31, 2012 

Test Methods Pollutant MDL 

used 

Emission 

Rate 

(lbs/hour) 

Emission 

Rate 

(lbs/ton) 

Emission 

Rate 

(mg/dscm) 

USEPA 

Method 5/29 Filterable PM < 1.1 x 10-1 1.3 

USEPA 

Method 29 

Filterable Chromium 

(FCr) < 1.2 x 10-5 1.4 x 10-4

Vaporous Chromium 

(VCr) < 3.8 x 10-6 4.3 x 10-5

Total Chromium (TCr) < 1.6 x 10-5 1.9 x 10-4

USEPA 

Method 0061 

Hexavalent Chromium 

(Cr+6) < 5.7 x 10-6 6.5 x 10-5

Total Chromium (TCr) < 1.1 x 10-4 1.2 x 10-3
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

iii

TABLE OF CONTENTS 

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

2.0 PROCESS DESCRIPTION ............................................................................................... 2

2.1 PROCESS MONITORING ....................................................................................................... 2

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

3.1 EXHAUST GAS VELOCITY, MOLECULAR WEIGHT, AND MOISTURE CONTENT .................... 2

3.2 PM, FCR, VCR, AND TCR CONCENTRATIONS AND EMISSION RATES ................................. 3

3.3 CR+6 AND TCR CONCENTRATIONS AND EMISSION RATES ................................................... 4

4.0 TEST RESULTS ................................................................................................................. 4

TABLES 

Table 1 – Test Personnel 

Table 2 – Overall Emission Test Results Summary – Line 122 North and South Combined 

Table 3 – Overall Emission Test Results Summary – Line 123 

Table 4 – Line 122, Melter Dust Collector – South Method 5/29 Emission Rate Results Summary 

Table 5 – Line 122, Melter Dust Collector – South Method 0061 Emission Rate Results Summary 

Table 6 – Line 122, Melter Dust Collector – North Method 5/29 Emission Rate Results Summary 

Table 7 – Line 122, Melter Dust Collector – North Method 0061 Emission Rate Results Summary 

Table 8 – Line 123 Dust Collector Method 5/29 Emission Rate Results Summary 

Table 9 – Line 123 Dust Collector Method 0061 Emission Rate Results Summary 

Table 10 – Line 122, Melter Dust Collector North and South Combined Method 5/29 Emission Rate Results Summary 

Table 11 – Line 122, Melter Dust Collector North and South Combined Method 0061 Emission Rate Results Summary 

FIGURES 

Figure 1 – Dust Collector Exhaust Stacks Traverse Point Diagram 

Figure 2 – Method 5/29 Sampling Train Schematic Drawing 

Figure 3 – Method 0061 Sampling Train Schematic Drawing 

APPENDICES 

Appendix A – Field and Computer Generated Raw Data and Field Notes 

Appendix B – Process Data 

Appendix C – Equipment Calibration Documents 

Appendix D – Laboratory Analytical Reports 
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

1

1.0 Introduction 

For the purpose of assisting in the development of any emission standard under Section 7412 of 

the Clean Air Act (CAA), Section 114 of the CAA gives the United States Environmental 

Protection Agency (U.S. EPA) authority to require that persons who operate any emission source 

“sample such emissions (in accordance with such procedures or methods, at such locations, at 

such intervals, during such periods and in such manner as the Administrator shall prescribe)”. 

Consistent with this authority, U.S. EPA has required that Johns Manville (JM) sample emissions 

for the purpose of providing residual risk-related data for the National Emission Standards for 

Hazardous Air Pollutants (NESHAP) for Wool Fiberglass Manufacturing2. 

To assist in collecting the agreed upon data, BT Environmental Consulting, Inc. (BTEC) was 

retained by JM to evaluate emission rates of the following pollutants from three exhaust stacks 

associated with the Line 122 Melter Dust Collector (2 stacks) and the Line 123 Melter Dust 

Collector (1 stack) located at the Johns Manville plant in McPherson, Kansas: 

• Filterable particulate matter (PM) using U.S. EPA Methods 5/29 

• Filterable chromium (FCr) using U.S. EPA Method 29 

• Vaporous chromium (VCr) using U.S. EPA Method 29 

• Total chromium (TCr) using U.S. EPA Method 29 

• Hexavalent chromium (Cr+6) using SW-846 Method 0061 

• TCr using SW-846 Method 0061 

The emissions test program was conducted on January 30 and 31 and February 1 and 2, 2012. 

The test program consisted of triplicate 240-minute emission tests for each parameter. The field 

sampling portion of the emissions test program included the personnel summarized by Table 1.

Table 1 

Emissions Test Program Personnel

Personnel Affiliation 

Barry Boulianne BTEC 

James Sharp BTEC 

Matthew Young BTEC 

Paul Draper BTEC 

Paul Molenda BTEC 

Brandon Chase 

Bill Eccles 

Ben Campbell 

Ron Hudson 

BTEC 

JM 

JM 

JM 

Scott Postma U.S. EPA 

Javier Ahumada KDHE 

 

2

 Codified at 40 CFR 63, Subpart NNN 
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

2

2.0 Process Description

Glass and cullet are fed to an electric-fired melter and melted to be formed into fiberglass. The 

three melters in Line 123 exhaust through a common baghouse. The two melters in Line 122 

exhaust into a common plenum that then splits into two baghouses, each with its own stack. A 

schematic drawing showing traverse point locations for each of three stacks evaluated is 

available as Figure 1. 

2.1 Process Monitoring 

Process and control equipment data collected during the emissions test program, as well as the 

frequency of data collection, included the following: 

1. Production Rate (lbs/hr), hourly 

4. Baghouse Pressure Drop, hourly 

Process production data is available in Appendix B. Control equipment data will be available to 

U.S. EPA on request. 

3.0 Sampling and Analytical Methodologies 

Sampling and analytical methodologies for the emissions test program can be separated into 

three categories as follows: 

(1) Measurement of exhaust gas velocity, molecular weight, and moisture content; 

(2) Measurement of exhaust gas PM, FCr, VCr, and TCr concentrations and emission rates 

using Methods 5/29; and 

(3) Measurement of exhaust gas CR+6 and TCr concentrations and emission rates using 

Method 0061. 

Descriptions of sampling and analytical methodologies by category are summarized by Sections 

3.1 through 3.3, respectively. 

3.1 Exhaust Gas Velocity, Molecular Weight, and Moisture Content 

Measurement of exhaust gas velocity, molecular weight, and moisture content were conducted 

using the following reference test methods codified at Title 40, Part 60, Appendix A of the Code 

of Federal Regulations (40 CFR 60, Appendix A): 

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

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

• Method 3A - “Determination of Molecular Weight of Dry Stack 

Gas”(Integrated tedlar bags)
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

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

These test methods were used to evaluate exhaust gas flowrates in conjunction with the 

isokinetic sampling methodologies. 

Stack gas velocity traverses were conducted in accordance with the procedures outlined in 

Method 1 and Method 2 (see Figure 1 for a traverse location drawing). An S-type pitot tube with 

a thermocouple assembly, calibrated in accordance with Method 2, Section 4.1.1, was used to 

measure exhaust gas velocity pressures (using a manometer) and temperatures at each location 

during testing. The S-type pitot tube dimensions was within specified limits, therefore, a 

baseline pitot tube coefficient of 0.84 (dimensionless) was assigned. 

Molecular weight was determined according to USEPA Method 3A, “Determination of Oxygen 

and Carbon Dioxide Concentrations in Emissions from Stationary Sources”. The O2 content of 

the exhaust gas was measured using an M&C Products PMA 100-L O2 gas analyzer and the CO2

content of the exhaust gas was measured using a California Analytical Instruments (CAI) 600 

Series CO2 gas analyzer. A sample of the gas stream was drawn through an insulated stainlesssteel probe into an integrated tedlar bag by the use of a vacuum sample lung. The sample was 

then connected to sample conditioner to remove the moisture from the sample before it entered 

the analyzers. Data was recorded at 4-second intervals on a PC equipped with data acquisition 

software. 

 

For O2 and CO2 analyzer calibrations, calibration gases were mixed to desired concentrations 

using an Environics Series 4040 Computerized Gas Dilution System. The Series 4040 consists 

of a single chassis with four mass flow controllers. The mass flow controllers are factorycalibrated using a primary flow standard traceable to the United State's National Institute of 

Standards and Technology (NIST). Each flow controller utilizes an 11-point calibration table 

with linear interpolation, to increase accuracy and reduce flow controller nonlinearity. 

Exhaust gas moisture content was evaluated using Method 4. Exhaust gas moisture content was 

determined gravimetrically. 

3.2 PM, FCr, VCr, and TCr Concentrations and Emission Rates

PM, FCr, VCr, and TCr concentrations and emission rates were measured using the procedures 

of 40 CFR 60, Appendix A, Methods 5 and 29. Selected metals concentrations and emission 

rates were measured using BTEC’s Nutech® Model 2010 modular isokinetic stack sampling 

system. This system consisted of (1) a borosilicate glass or quartz nozzle, (2) a steel probe 

w/glass liner, (3) a heated quartz fiber filter assembly, (4) a set of four GS impingers, (5) a 

length of sample line, and (6) a Nutech® control case equipped with a pump, dry gas meter, and 

calibrated orifice. Prior to each test, the first two impingers were filled with 100 ml of a 5% 

nitric acid (HNO3)/10% hydrogen peroxide solution, the third impinger was empty, and the 

fourth contained approximately 300 g of silica gel desiccant. A schematic drawing of the 

PM/metals sampling train is provided as Figure 2. 
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

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3.3 Cr+6 and TCr Concentrations and Emission Rates 

Measurement of Cr+6 and TCr concentrations and emission rates were measured using the 

procedures of Method 0061. Cr+6 and TCr concentrations and emission rates were measured 

using BTEC’s Nutech® Model 2010 modular isokinetic stack sampling system. This system 

consisted of (1) a glass nozzle, (2) a heated steel probe with a glass probe liner, (4) a Teflon tee 

with a recirculating pump, (5) five GS impingers, (6) a length of sample line, and (7) a Nutech®

control case equipped with a pump, dry gas meter, and calibrated orifice. Prior to each test, the 

first impinger was filled with 150 mL of 0.1N KOH, the next two were filled with 75 mL of 0.1 

N KOH, the fourth was empty, and the last impinger contained approximately 300 g of silica gel 

desiccant. A schematic drawing of the Method 0061 sampling train is provided as Figure 3. 

4.0 Test Results 

The overall results of the emissions test program are summarized by Tables 2 and 3. 

Table 2 

Overall Emissions Test Results Summary 

Line 122 Melter Dust Collector North and South 

Test Dates: February 1 and 2, 2012 

Test Methods Pollutant MDL 

used 

Emission 

Rate 

(lbs/hour) 

Emission 

Rate 

(lbs/ton) 

Emission 

Rate 

(mg/dscm) 

USEPA 

Method 5/29 Filterable PM < 1.5 x 10-1 9.5 x 10-1 

USEPA 

Method 29 

Filterable Chromium 

(FCr) < 1.3 x 10-4 8.8 x 10-4

Vaporous Chromium 

(VCr) < 5.6 x 10-6 3.5 x 10-5

Total Chromium (TCr) < 1.4 x 10-4 9.2 x 10-4

USEPA 

Method 0061 

Hexavalent Chromium 

(Cr+6) < 1.1 x 10-5 6.9 x 10-5

Total Chromium (TCr) < 1.8 x 10-4 1.2 x 10-3
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

5

Table 3 

Overall Emissions Test Results Summary 

Line 123 Melter Dust Collector 

Test Dates: January 30 and 31, 2012 

Test Methods Pollutant MDL 

used 

Emission 

Rate 

(lbs/hour) 

Emission 

Rate 

(lbs/ton) 

Emission 

Rate 

(mg/dscm) 

USEPA 

Method 5/29 Filterable PM < 1.1 x 10-1 1.3 

USEPA 

Method 29 

Filterable Chromium 

(FCr) < 1.2 x 10-5 1.4 x 10-4

Vaporous Chromium 

(VCr) < 3.8 x 10-6 4.3 x 10-5

Total Chromium (TCr) < 1.6 x 10-5 1.9 x 10-4

USEPA 

Method 0061 

Hexavalent Chromium 

(Cr+6) < 5.7 x 10-6 6.5 x 10-5

Total Chromium (TCr) < 1.1 x 10-4 1.2 x 10-3

Detailed results for individual emission test runs are summarized in Tables 4 through 11. Field 

and computer-generated data sheets are included in Appendix A. Process data associated with the 

emissions test program is provided in Appendix B. Equipment calibration documents are 

provided in Appendix C. Laboratory analytical results are available in Appendix D. 
Johns Manville McPherson BTEC Project No. 11-4191.03 

U.S. EPA Emissions Test Report February 22, 2012 

6

Limitations 

The information and opinions rendered in this report are exclusively for use by Johns Manville. 

BTEC will not distribute or publish this report without Johns Manville’s consent except as 

required by law or court order. BTEC accepts responsibility for the competent performance of 

its duties in executing the assignment and preparing reports in accordance with the normal 

standards of the profession, but disclaims any responsibility for consequential damages. 

This report was prepared by: 

Brandon Chase 

Staff Environmental Engineer 

This report was reviewed by: 

Randal J. Tysar 

Senior Environmental Engineer 
Tables 
Table 4

Line 122, Melter Dust Collector - South Method 5/29 Emission Rate Results Summary

Company JM McPherson

Source Designation 122 M1 DC

Test Date 2/1/2012 2/1/2012 2/2/2012

Meter/Nozzle Information P-1 P-2 P-3 Average

Meter Temperature Tm (F) 61.0 79.1 56.6 65.6

Meter Pressure - Pm (in. Hg) 30.2 30.2 30.3 30.3

Measured Sample Volume (Vm) 170.1 172.7 165.4 169.4

Sample Volume (Vm-Std ft3) 174.5 171.3 171.6 172.5

Sample Volume (Vm-Std m3) 4.94 4.85 4.86 4.88

Condensate Volume (Vw-std) 2.060 2.018 2.603 2.227

Gas Density (Ps(std) lbs/ft3) (wet) 0.0742 0.0742 0.0741 0.0742

Gas Density (Ps(std) lbs/ft3) (dry) 0.0745 0.0745 0.0745 0.0745

Total weight of sampled gas (m g lbs) (wet) 13.10 12.86 12.91 12.95

Total weight of sampled gas (m g lbs) (dry) 13.00 12.76 12.78 12.85

Nozzle Size - An (sq. ft.) 0.000262 0.000262 0.000262 0.000262

Isokinetic Variation - I 100.5 100.5 100.2 100.4

Production Data

Production Data (lb/hr)

Stack Data

Average Stack Temperature - Ts (F) 112.0 129.3 114.0 118.4

Molecular Weight Stack Gas- dry (Md) 28.8 28.8 28.8 28.8

Molecular Weight Stack Gas-wet (Ms) 28.7 28.7 28.7 28.7

Stack Gas Specific Gravity (Gs) 0.991 0.991 0.990 0.991

Percent Moisture (Bws) 1.17 1.16 1.49 1.28

Water Vapor Volume (fraction) 0.0117 0.0116 0.0149 0.0128

Pressure - Ps ("Hg) 30.1 30.1 30.2 30.1

Average Stack Velocity -Vs (ft/sec) 50.2 50.8 49.8 50.3

Area of Stack (ft2) 7.9 7.9 7.9 7.9

Exhaust Gas Flowrate

Flowrate ft3

(Actual) 23,731 23,989 23,498 23,739

Flowrate ft3

 (Standard Wet) 22,032 21,616 21,799 21,816

Flowrate ft3

 (Standard Dry) 21,775 21,365 21,473 21,538

Flowrate m3

 (standard dry) 617 605 608 610

Total Particulate Weights (mg)

Acetone Rinse 5.4 3.8 2.9 4.0

Filter < 0.3 < 0.3 < 0.3 0.3

Total < 5.7 < 4.1 < 3.2 4.3

Total Particulate Concentration

 lb/1000 lb (wet) < 9.6E-04 < 7.0E-04 < 5.5E-04 7.4E-04

 lb/1000 lb (dry) < 9.7E-04 < 7.1E-04 < 5.5E-04 7.4E-04

mg/dscm (dry) < 1.2E+00 < 8.5E-01 < 6.6E-01 8.9E-01

gr/dscf < 5.0E-04 < 3.7E-04 < 2.9E-04 3.9E-04

Total Particulate Emission Rate

 lb/ hr < 9.4E-02 < 6.8E-02 < 5.3E-02 7.2E-02

 lb/ ton product

Filterable Chromium Weights (ug)

Front Half Chromium (Filterable) 1.98 9.75 9.75 7.16

Filterable Chromium Concentrations

 lb/1000 lb (wet) 3.3E-07 1.7E-06 1.7E-06 1.2E-06

 lb/1000 lb (dry) 3.4E-07 1.7E-06 1.7E-06 1.2E-06

mg/dscm (dry) 4.0E-04 2.0E-03 2.0E-03 1.5E-03

gr/dscf 1.8E-07 8.8E-07 8.8E-07 6.4E-07

Filterable Chromium Emission Rate

 lb/ hr 3.3E-05 1.6E-04 1.6E-04 1.2E-04

 lb/ ton product

Vaporous Chromium Weights (ug)

Back Half Chromium (Vaporous) < 0.15 0.22 < 0.15 0.17

Vaporous Chromium Concentrations

 lb/1000 lb (wet) < 2.5E-08 < 3.8E-08 < 2.6E-08 3.0E-08

 lb/1000 lb (dry) < 2.5E-08 < 3.8E-08 < 2.6E-08 3.0E-08

mg/dscm (dry) < 3.0E-05 < 4.5E-05 < 3.1E-05 3.6E-05

gr/dscf < 1.3E-08 < 2.0E-08 < 1.3E-08 1.6E-08

Vaporous Chromium Emission Rate

 lb/ hr < 2.5E-06 < 3.6E-06 < 2.5E-06 2.9E-06

 lb/ ton product

Total Chromium Weights (ug)

Total Chromium < 2.13 9.97 < 9.90 7.33

Total Chromium Concentrations

 lb/1000 lb (wet) < 3.6E-07 < 1.7E-06 < 1.7E-06 1.3E-06

 lb/1000 lb (dry) < 3.6E-07 < 1.7E-06 < 1.7E-06 1.3E-06

mg/dscm (dry) < 4.3E-04 < 2.1E-03 < 2.0E-03 1.5E-03

gr/dscf < 1.9E-07 < 9.0E-07 < 8.9E-07 6.6E-07

Total Chromium Emission Rate

 lb/ hr < 3.5E-05 < 1.7E-04 < 1.6E-04 1.2E-04

 lb/ ton product
Table 5

Line 122, Melter Dust Collector - South Method 0061 Emission Rate Results Summary

Company JM McPherson

Source Designation 122 M1 DC

Test Date 2/1/2012 2/1/2012 2/2/2012

Meter/Nozzle Information P-1 P-2 P-3 Average

Meter Temperature Tm (F) 60.8 78.5 53.7 64.3

Meter Pressure - Pm (in. Hg) 30.2 30.2 30.3 30.3

Measured Sample Volume (Vm) 157.4 164.4 155.6 159.1

Sample Volume (Vm-Std ft3) 162.2 163.9 163.0 163.0

Sample Volume (Vm-Std m3) 4.59 4.64 4.62 4.62

Condensate Volume (Vw-std) 2.296 2.810 1.565 2.224

Gas Density (Ps(std) lbs/ft3) (wet) 0.0741 0.0740 0.0742 0.0741

Gas Density (Ps(std) lbs/ft3) (dry) 0.0745 0.0745 0.0745 0.0745

Total weight of sampled gas (m g lbs) (wet) 12.19 12.34 12.22 12.25

Total weight of sampled gas (m g lbs) (dry) 12.09 12.21 12.14 12.15

Nozzle Size - An (sq. ft.) 0.000257 0.000257 0.000257 0.000257

Isokinetic Variation - I 99.5 99.6 99.2 99.4

Production Data

Production Data (lb/hr)

Stack Data

Average Stack Temperature - Ts (F) 108.8 124.4 110.5 114.6

Oxygen Concentration (%) 20.7 20.7 20.7

Molecular Weight Stack Gas- dry (Md) 28.8 28.8 28.8 28.8

Molecular Weight Stack Gas-wet (Ms) 28.7 28.6 28.7 28.7

Stack Gas Specific Gravity (Gs) 0.990 0.989 0.992 0.990

Percent Moisture (Bws) 1.40 1.69 0.95 1.34

Water Vapor Volume (fraction) 0.0140 0.0169 0.0095 0.0134

Pressure - Ps ("Hg) 30.1 30.1 30.2 30.1

Average Stack Velocity -Vs (ft/sec) 47.9 49.8 48.1 48.6

Area of Stack (ft2) 7.9 7.9 7.9 7.9

Exhaust Gas Flowrate

Flowrate ft3

(Actual) 22,628 23,526 22,701 22,952

Flowrate ft3

 (Standard Wet) 21,125 21,379 21,186 21,230

Flowrate ft3

 (Standard Dry) 20,830 21,019 20,985 20,945

Flowrate m3

 (standard dry) 590 595 594 593

Total Hexavalent Chromium Weight (ug)

Hexavalent Chromium < 0.40 < 0.30 < 0.30 0.33

Total Hexavalent Chromium Concentration

 lb/1000 lb (wet) < 7.2E-08 < 5.4E-08 < 5.4E-08 6.0E-08

 lb/1000 lb (dry) < 7.3E-08 < 5.4E-08 < 5.4E-08 6.1E-08

mg/dscm (dry) < 8.7E-05 < 6.5E-05 < 6.5E-05 7.2E-05

Total Hexavalent Chromium Emission Rate

 lb/ hr < 6.8E-06 < 5.1E-06 < 5.1E-06 5.7E-06

 lb/ ton product

Total Chromium Weight (ug)

Back Half Chromium < 4.00 < 3.00 < 4.00 3.67

Front Half Chromium < 0.30 < 0.30 < 0.30 0.30

Rinse Chromium < 2.00 < 2.00 < 2.00

Total Chromium < 6.30 < 5.30 < 6.30 5.97

Total Chromium Concentration

 lb/1000 lb (wet) < 1.1E-06 < 9.5E-07 < 1.1E-06 1.1E-06

 lb/1000 lb (dry) < 1.1E-06 < 9.6E-07 < 1.1E-06 1.1E-06

mg/dscm (dry) < 1.4E-03 < 1.1E-03 < 1.4E-03 1.3E-03

Total Chromium Emission Rate

 lb/ hr < 1.07E-04 < 9.0E-05 < 1.1E-04 1.0E-04

 lb/ ton product
Table 6

Line 122, Melter Dust Collector - North Method 5/29 Emission Rate Results Summary

Company JM McPherson

Source Designation 122 M2 Dust (M29)

Test Date 2/1/2012 2/1/2012 2/2/2012

Meter/Nozzle Information P-1 P-2 P-3 Average

Meter Temperature Tm (F) 62.7 83.2 55.9 67.3

Meter Pressure - Pm (in. Hg) 30.2 30.2 30.3 30.3

Measured Sample Volume (Vm) 150.3 153.0 151.3 151.5

Sample Volume (Vm-Std ft3) 153.1 150.0 156.5 153.2

Sample Volume (Vm-Std m3) 4.34 4.25 4.43 4.34

Condensate Volume (Vw-std) 1.763 1.622 1.636 1.674

Gas Density (Ps(std) lbs/ft3) (wet) 0.0742 0.0742 0.0742 0.0742

Gas Density (Ps(std) lbs/ft3) (dry) 0.0745 0.0745 0.0745 0.0745

Total weight of sampled gas (m g lbs) (wet) 11.49 11.25 11.74 11.49

Total weight of sampled gas (m g lbs) (dry) 11.41 11.17 11.66 11.41

Nozzle Size - An (sq. ft.) 0.000247 0.000247 0.000247 0.000247

Isokinetic Variation - I 99.4 99.2 99.3 99.3

Production Data

Production Data (lb/hr)

Stack Data

Average Stack Temperature - Ts (F) 103.2 113.1 97.0 104.4

Molecular Weight Stack Gas- dry (Md) 28.8 28.8 28.8 28.8

Molecular Weight Stack Gas-wet (Ms) 28.7 28.7 28.7 28.7

Stack Gas Specific Gravity (Gs) 0.991 0.991 0.992 0.991

Percent Moisture (Bws) 1.14 1.07 1.03 1.08

Water Vapor Volume (fraction) 0.0114 0.0107 0.0103 0.0108

Pressure - Ps ("Hg) 30.1 30.1 30.2 30.1

Average Stack Velocity -Vs (ft/sec) 46.3 46.2 46.7 46.4

Area of Stack (ft2) 7.9 7.9 7.9 7.9

Exhaust Gas Flowrate

Flowrate ft3

(Actual) 21,885 21,843 22,070 21,933

Flowrate ft3

 (Standard Wet) 20,648 20,252 21,104 20,668

Flowrate ft3

 (Standard Dry) 20,413 20,035 20,885 20,444

Flowrate m3

 (standard dry) 578 567 591 579

Total Particulate Weights (mg)

Acetone Rinse 4.6 3.2 4.6 4.1

Filter < 0.3 < 0.3 < 0.3 0.3

Total < 4.9 < 3.5 < 4.9 4.4

Total Particulate Concentration

 lb/1000 lb (wet) < 9.4E-04 < 6.9E-04 < 9.2E-04 8.5E-04

 lb/1000 lb (dry) < 9.5E-04 < 6.9E-04 < 9.3E-04 8.5E-04

mg/dscm (dry) < 1.1E+00 < 8.2E-01 < 1.1E+00 1.0E+00

gr/dscf < 4.9E-04 < 3.6E-04 < 4.8E-04 4.5E-04

Total Particulate Emission Rate

 lb/ hr < 8.7E-02 < 6.2E-02 < 8.7E-02 7.9E-02

 lb/ ton product

Filterable Chromium Weights (ug)

Front Half Chromium (Filterable) 1.54 0.76 < 0.60 0.97

Filterable Chromium Concentrations

 lb/1000 lb (wet) 3.0E-07 1.5E-07 < 1.1E-07 1.9E-07

 lb/1000 lb (dry) 3.0E-07 1.5E-07 < 1.1E-07 1.9E-07

mg/dscm (dry) 3.6E-04 1.8E-04 < 1.4E-04 2.2E-04

gr/dscf 1.6E-07 7.8E-08 < 5.9E-08 9.8E-08

Filterable Chromium Emission Rate

 lb/ hr 2.7E-05 1.3E-05 < 1.1E-05 1.7E-05

 lb/ ton product

Vaporous Chromium Weights (ug)

Back Half Chromium (Vaporous) < 0.15 < 0.15 < 0.15 0.15

Vaporous Chromium Concentrations

 lb/1000 lb (wet) < 2.9E-08 < 2.9E-08 < 2.8E-08 2.9E-08

 lb/1000 lb (dry) < 2.9E-08 < 3.0E-08 < 2.8E-08 2.9E-08

mg/dscm (dry) < 3.5E-05 < 3.5E-05 < 3.4E-05 3.5E-05

gr/dscf < 1.5E-08 < 1.5E-08 < 1.5E-08 1.5E-08

Vaporous Chromium Emission Rate

 lb/ hr < 2.7E-06 < 2.7E-06 < 2.7E-06 2.7E-06

 lb/ ton product

Total Chromium Weights (ug)

Total Chromium < 1.69 < 0.91 < 0.75 1.12

Total Chromium Concentrations

 lb/1000 lb (wet) < 3.2E-07 < 1.8E-07 < 1.4E-07 2.1E-07

 lb/1000 lb (dry) < 3.3E-07 < 1.8E-07 < 1.4E-07 2.2E-07

mg/dscm (dry) < 3.9E-04 < 2.1E-04 < 1.7E-04 2.6E-04

gr/dscf < 1.7E-07 < 9.4E-08 < 7.4E-08 1.1E-07

Total Chromium Emission Rate

 lb/ hr < 3.0E-05 < 1.6E-05 < 1.3E-05 2.0E-05

 lb/ ton product
Table 7

Line 122, Melter Dust Collector - North Method 0061 Emission Rate Results Summary

Company JM Mcpherson

Source Designation M-2 dust collector

Test Date 2/1/2012 2/1/2012 2/1/2012

Meter/Nozzle Information P-1 P-2 P-3 Average

Meter Temperature Tm (F) 59.9 79.4 51.9 63.7

Meter Pressure - Pm (in. Hg) 30.2 30.2 30.3 30.3

Measured Sample Volume (Vm) 154.2 159.4 157.1 156.9

Sample Volume (Vm-Std ft3) 159.0 158.4 164.9 160.8

Sample Volume (Vm-Std m3) 4.50 4.49 4.67 4.55

Condensate Volume (Vw-std) 2.197 2.084 1.985 2.089

Gas Density (Ps(std) lbs/ft3) (wet) 0.0741 0.0741 0.0742 0.0741

Gas Density (Ps(std) lbs/ft3) (dry) 0.0745 0.0745 0.0745 0.0745

Total weight of sampled gas (m g lbs) (wet) 11.95 11.90 12.38 12.08

Total weight of sampled gas (m g lbs) (dry) 11.85 11.80 12.29 11.98

Nozzle Size - An (sq. ft.) 0.000254 0.000254 0.000254 0.000254

Isokinetic Variation - I 100.3 99.7 100.6 100.2

Production Data

Production Data (lb/hr)

Stack Data

Average Stack Temperature - Ts (F) 103.6 112.9 97.8 104.8

Oxygen Concentration (%) 20.7 20.7 20.7

Molecular Weight Stack Gas- dry (Md) 28.8 28.8 28.8 28.8

Molecular Weight Stack Gas-wet (Ms) 28.7 28.7 28.7 28.7

Stack Gas Specific Gravity (Gs) 0.990 0.991 0.991 0.991

Percent Moisture (Bws) 1.36 1.30 1.19 1.28

Water Vapor Volume (fraction) 0.0136 0.0130 0.0119 0.0128

Pressure - Ps ("Hg) 30.1 30.1 30.2 30.1

Average Stack Velocity -Vs (ft/sec) 46.5 47.4 47.4 47.1

Area of Stack (ft2) 7.9 7.9 7.9 7.9

Exhaust Gas Flowrate

Flowrate ft3

(Actual) 21,981 22,387 22,386 22,251

Flowrate ft3

 (Standard Wet) 20,716 20,756 21,375 20,949

Flowrate ft3

 (Standard Dry) 20,434 20,486 21,121 20,680

Flowrate m3

 (standard dry) 579 580 598 586

Total Hexavalent Chromium Weight (ug)

Hexavalent Chromium < 0.30 < 0.30 < 0.30 0.30

Total Hexavalent Chromium Concentration

 lb/1000 lb (wet) < 5.5E-08 < 5.6E-08 < 5.3E-08 5.5E-08

 lb/1000 lb (dry) < 5.6E-08 < 5.6E-08 < 5.4E-08 5.5E-08

mg/dscm (dry) < 6.7E-05 < 6.7E-05 < 6.4E-05 6.6E-05

Total Hexavalent Chromium Emission Rate

 lb/ hr < 5.1E-06 < 5.2E-06 < 5.1E-06 5.1E-06

 lb/ ton product

Total Chromium Weight (ug)

Back Half Chromium < 4.00 < 4.00 < 4.00 4.00

Front Half Chromium < 0.30 < 0.30 < 0.30 0.30

Rinse Chromium < 0.30 < 0.30 < 0.30

Total Chromium < 4.60 < 4.60 < 4.60 4.60

Total Chromium Concentration

 lb/1000 lb (wet) < 8.5E-07 < 8.5E-07 < 8.2E-07 8.4E-07

 lb/1000 lb (dry) < 8.6E-07 < 8.6E-07 < 8.3E-07 8.5E-07

mg/dscm (dry) < 1.0E-03 < 1.0E-03 < 9.9E-04 1.0E-03

Total Chromium Emission Rate

 lb/ hr < 7.8E-05 < 7.9E-05 < 7.8E-05 7.9E-05

 lb/ ton product
Table 8

Line 123 Dust Collector Method 5/29 Emission Rate Results Summary

Company JM McPherson

Source Designation 123 (M29)

Test Date 1/30/2012 1/31/2012 1/31/2012

Meter/Nozzle Information P-1 P-2 P-3 Average

Meter Temperature Tm (F) 74.4 66.0 88.6 76.3

Meter Pressure - Pm (in. Hg) 30.1 30.0 30.0 30.0

Measured Sample Volume (Vm) 178.1 172.6 191.2 180.6

Sample Volume (Vm-Std ft3) 176.8 173.2 184.1 178.0

Sample Volume (Vm-Std m3) 5.01 4.90 5.21 5.04

Condensate Volume (Vw-std) 3.267 3.239 3.234 3.247

Gas Density (Ps(std) lbs/ft3) (wet) 0.0740 0.0740 0.0740 0.0740

Gas Density (Ps(std) lbs/ft3) (dry) 0.0745 0.0745 0.0745 0.0745

Total weight of sampled gas (m g lbs) (wet) 13.33 13.06 13.87 13.42

Total weight of sampled gas (m g lbs) (dry) 13.17 12.91 13.72 13.27

Nozzle Size - An (sq. ft.) 0.000252 0.000252 0.000247 0.000251

Isokinetic Variation - I 99.9 99.7 99.8 99.8

Production Data

Production Data (lb/hr)

Stack Data

Average Stack Temperature - Ts (F) 123.4 112.6 125.7 120.6

Molecular Weight Stack Gas- dry (Md) 28.8 28.8 28.8 28.8

Molecular Weight Stack Gas-wet (Ms) 28.6 28.6 28.6 28.6

Stack Gas Specific Gravity (Gs) 0.989 0.989 0.989 0.989

Percent Moisture (Bws) 1.82 1.84 1.73 1.79

Water Vapor Volume (fraction) 0.0182 0.0184 0.0173 0.0179

Pressure - Ps ("Hg) 29.9 29.8 29.8 29.9

Average Stack Velocity -Vs (ft/sec) 54.8 53.1 58.7 55.5

Area of Stack (ft2) 7.9 7.9 7.9 7.9

Exhaust Gas Flowrate

Flowrate ft3

(Actual) 25,889 25,071 27,723 26,227

Flowrate ft3

 (Standard Wet) 23,451 23,028 24,897 23,792

Flowrate ft3

 (Standard Dry) 23,025 22,605 24,467 23,365

Flowrate m3

 (standard dry) 652 640 693 662

Total Particulate Weights (mg)

Acetone Rinse 4.9 11.1 2.2 6.1

Filter < 0.3 < 0.3 < 0.3 0.3

Total < 5.2 < 11.4 < 2.5 6.4

Total Particulate Concentration

 lb/1000 lb (wet) < 8.6E-04 < 1.9E-03 < 4.0E-04 1.1E-03

 lb/1000 lb (dry) < 8.7E-04 < 1.9E-03 < 4.0E-04 1.1E-03

mg/dscm (dry) < 1.0E+00 < 2.3E+00 < 4.8E-01 1.3E+00

gr/dscf < 4.5E-04 < 1.0E-03 < 2.1E-04 5.6E-04

Total Particulate Emission Rate

 lb/ hr < 9.0E-02 < 2.0E-01 < 4.4E-02 1.1E-01

 lb/ ton product

Filterable Chromium Weights (ug)

Front Half Chromium (Filterable) < 0.60 0.94 < 0.60 0.71

Filterable Chromium Concentrations

 lb/1000 lb (wet) < 9.9E-08 1.6E-07 < 9.5E-08 1.2E-07

 lb/1000 lb (dry) < 1.0E-07 1.6E-07 < 9.6E-08 1.2E-07

mg/dscm (dry) < 1.2E-04 1.9E-04 < 1.2E-04 1.4E-04

gr/dscf < 5.2E-08 8.4E-08 < 5.0E-08 6.2E-08

Filterable Chromium Emission Rate

 lb/ hr < 1.0E-05 1.6E-05 < 1.1E-05 1.2E-05

 lb/ ton product

Vaporous Chromium Weights (ug)

Back Half Chromium (Vaporous) 0.35 < 0.15 < 0.15 0.22

Vaporous Chromium Concentrations

 lb/1000 lb (wet) 5.8E-08 < 2.5E-08 < 2.4E-08 3.6E-08

 lb/1000 lb (dry) 5.9E-08 < 2.6E-08 < 2.4E-08 3.6E-08

mg/dscm (dry) 7.0E-05 < 3.1E-05 < 2.9E-05 4.3E-05

gr/dscf 3.1E-08 < 1.3E-08 < 1.3E-08 1.9E-08

Vaporous Chromium Emission Rate

 lb/ hr < 6.1E-06 < 2.6E-06 < 2.6E-06 3.8E-06

 lb/ ton product

Total Chromium Weights (ug)

Total Chromium < 0.95 < 1.09 < 0.75 0.93

Total Chromium Concentrations

 lb/1000 lb (wet) < 1.6E-07 < 1.8E-07 < 1.2E-07 1.5E-07

 lb/1000 lb (dry) < 1.6E-07 < 1.9E-07 < 1.2E-07 1.6E-07

mg/dscm (dry) < 1.9E-04 < 2.2E-04 < 1.4E-04 1.9E-04

gr/dscf < 8.3E-08 < 9.7E-08 < 6.3E-08 8.1E-08

Total Chromium Emission Rate

 lb/ hr < 1.6E-05 < 1.9E-05 < 1.3E-05 1.6E-05

 lb/ ton product
Table 9

Line 123 Dust Collector Method 0061 Emission Rate Results Summary

Company JM McPherson

Source Designation 123 DC

Test Date 1/30/2012 1/31/2012 1/31/2012

Meter/Nozzle Information P-1 P-2 P-3 Average

Meter Temperature Tm (F) 69.9 62.5 79.4 70.6

Meter Pressure - Pm (in. Hg) 30.1 30.0 30.0 30.0

Measured Sample Volume (Vm) 175.5 175.4 187.2 179.4

Sample Volume (Vm-Std ft3) 177.0 178.7 184.7 180.1

Sample Volume (Vm-Std m3) 5.01 5.06 5.23 5.10

Condensate Volume (Vw-std) 3.447 3.456 3.420 3.441

Gas Density (Ps(std) lbs/ft3) (wet) 0.0741 0.0741 0.0741 0.0741

Gas Density (Ps(std) lbs/ft3) (dry) 0.0746 0.0746 0.0746 0.0746

Total weight of sampled gas (m g lbs) (wet) 13.37 13.49 13.94 13.60

Total weight of sampled gas (m g lbs) (dry) 13.21 13.33 13.78 13.44

Nozzle Size - An (sq. ft.) 0.000254 0.000254 0.000254 0.000254

Isokinetic Variation - I 100.1 99.7 99.9 99.9

Production Data

Production Data (lb/hr)

Stack Data

Average Stack Temperature - Ts (F) 121.1 110.9 122.5 118.2

Oxygen Concentration (%) 20.5 20.5 20.5

Molecular Weight Stack Gas- dry (Md) 28.9 28.9 28.9 28.9

Molecular Weight Stack Gas-wet (Ms) 28.7 28.7 28.7 28.7

Stack Gas Specific Gravity (Gs) 0.989 0.989 0.990 0.990

Percent Moisture (Bws) 1.91 1.90 1.82 1.88

Water Vapor Volume (fraction) 0.0191 0.0190 0.0182 0.0188

Pressure - Ps ("Hg) 29.9 29.8 29.8 29.9

Average Stack Velocity -Vs (ft/sec) 54.1 54.1 56.9 55.0

Area of Stack (ft2) 7.9 7.9 7.9 7.9

Exhaust Gas Flowrate

Flowrate ft3

(Actual) 25,554 25,552 26,881 25,996

Flowrate ft3

 (Standard Wet) 23,239 23,540 24,272 23,684

Flowrate ft3

 (Standard Dry) 22,795 23,093 23,831 23,240

Flowrate m3

 (standard dry) 645 654 675 658

Total Hexavalent Chromium Weight (ug)

Hexavalent Chromium < 0.30 < 0.40 < 0.30 0.33

Total Hexavalent Chromium Concentration

 lb/1000 lb (wet) < 4.9E-08 < 6.5E-08 < 4.7E-08 5.4E-08

 lb/1000 lb (dry) < 5.0E-08 < 6.6E-08 < 4.8E-08 5.5E-08

mg/dscm (dry) < 6.0E-05 < 7.9E-05 < 5.7E-05 6.5E-05

Total Hexavalent Chromium Emission Rate

 lb/ hr < 5.1E-06 < 6.9E-06 < 5.1E-06 5.7E-06

 lb/ ton product

Total Chromium Weight (ug)

Back Half Chromium < 4.00 < 5.00 < 4.00 4.33

Front Half Chromium < 0.30 < 0.30 < 0.30 0.30

Rinse Chromium < 2.00 < 1.00 < 2.00

Total Chromium < 6.30 < 6.30 < 6.30 6.30

Total Chromium Concentration

 lb/1000 lb (wet) < 1.0E-06 < 1.0E-06 < 1.0E-06 1.0E-06

 lb/1000 lb (dry) < 1.1E-06 < 1.0E-06 < 1.0E-06 1.0E-06

mg/dscm (dry) < 1.3E-03 < 1.2E-03 < 1.2E-03 1.2E-03

Total Chromium Emission Rate

 lb/ hr < 1.1E-04 < 1.1E-04 < 1.1E-04 1.1E-04

 lb/ ton product
Table 10

Line 122, Melter Dust Collector - North and South Method 5/29 Emission Rate Results Summary

Company JM McPherson

Source Designation 122 Combined

Test Date 2/1/2012 2/1/2012 2/2/2012

Production Data Run 1 Run 2 Run 3

Production Data (lb/hr)

Total Particulate Concentration

mg/dscm (dry) < 1.1E+00 < 8.4E-01 < 8.7E-01 9.5E-01

Total Particulate Emission Rate

 lb/ hr < 1.8E-01 < 1.3E-01 < 1.4E-01 1.5E-01

 lb/ ton product

Filterable Chromium Concentrations

mg/dscm (dry) 3.8E-04 1.2E-03 1.1E-03 8.8E-04

Filterable Chromium Emission Rate

 lb/ hr 6.0E-05 1.7E-04 1.7E-04 1.3E-04

 lb/ ton product

Vaporous Chromium Concentrations

mg/dscm (dry) < 3.2E-05 < 4.1E-05 < 3.2E-05 3.5E-05

Vaporous Chromium Emission Rate

 lb/ hr < 5.2E-06 < 6.3E-06 < 5.2E-06 5.6E-06

 lb/ ton product

Total Chromium Concentrations

mg/dscm (dry) < 4.1E-04 < 1.2E-03 < 1.1E-03 9.2E-04

Total Chromium Emission Rate

 lb/ hr < 6.5E-05 < 1.9E-04 < 1.7E-04 1.4E-04

 lb/ ton product
Table 11

Line 122, Melter Dust Collector - North and South Method 0061 Emission Rate Results Summary

Company JM McPherson

Source Designation 122 Combined

Test Date 2/1/2012 2/1/2012 2/2/2012

Production Data Run 1 Run 2 Run 3

Production Data (lb/hr)

Total Hexavalent Chromium Concentration

mg/dscm (dry) < 7.7E-05 < 6.6E-05 < 6.5E-05 6.9E-05

Total Hexavalent Chromium Emission Rate

 lb/ hr < 1.2E-05 < 1.0E-05 < 1.0E-05 1.1E-05

 lb/ ton product

Total Chromium Concentration

mg/dscm (dry) < 1.2E-03 < 1.1E-03 < 1.2E-03 1.2E-03

Total Chromium Emission Rate

 lb/ hr < 1.85E-04 < 1.69E-04 < 1.88E-04 1.8E-04

 lb/ ton product
Figures 
diameter = 38"

Points Distance "

12 0.8

11 2.5

10 4.5

9 6.7

8 9.5

7 13.5

6 24.5

5 28.5

4 31.3

3 33.5

2 35.5

1 37.2

Figure 1

Site:

Johns Manville

McPherson, Kansas

Lines 122 and 123 Melters (3 stacks)

BT Environmental Consulting, 

Inc.

4949 Fernlee Ave

Royal Oak, Michigan

Not to Scale 

<0.5 diameters 

<2 diameters 
Figure 2

Site:USEPA Methods 5/29Johns ManvilleMcPherson, Kansas

BT Environmental Consult4949 Fernlee AvenueRoyal Oak, Michigan

Silica gel 

100 mL 5% HNO3 / 10% H2O2 solution 

Heated Filter Box 

S-Type Pitot w/ Thermocouple 

Heated Probe w/ Glass Liner & Nozzle 

Meter Rig 

Temp. 

Probe

Filter 

On 

Off -+

00:00 

1 2 3 4 5 
Figure 3

Site:USEPA Method 0061Johns ManvilleMcPherson, KS

BT Environmental Cons4949 Fernlee AvenueRoyal Oak, Michigan

Meter Rig 

Temp. 

Probe

Filter 

On 

Off -+

00:00 

1 2 3 4 5 

150 mL 0.1 N KOH Empty Silica Gel 

Perastaltic pump 

Teflon tee 

75 mL 0.1 N KOH 
Appendix A 

Field and Computer Generated Raw Data and Field Notes 
Company JM McPherson

Source Designation 122 M1 DCTest Date 2/1/2012 Assumed Moisture (Bws) 2

Test Number M5-29 R1 Condensate Volume (Vlc) 11.9Operator BC/PD Silica Gel Weight Gain (Vlc) 31.8Filter Number 11081872 Nozzle Diameter (in.) 0.219Barometric Pressure (Pb) 30.13 Leak Rate Initial 0.000 @ 15"Stack Static Pressure (Pg) -0.51 Leak Rate Final 0.000 @ 7"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84Pitot Tube Number 5'B Meter Corr. Factor (Y) 1.002Meter Number MB-5 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0Delta ∆H@ 1.55 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Actual Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (

1 0 8:06 3 110 0.80 1.50 1.45 930.11 42 42 38 253 245 2 5 3 110 0.85 1.59 1.54 933.71 43 42 39 252 250 3 10 3 110 0.85 1.59 1.54 937.41 44 42 38 245 251 4 15 3 110 0.84 1.57 1.50 941.12 45 42 39 252 251 5 20 3 110 0.82 1.53 1.50 944.74 49 43 41 256 250 6 25 3 109 0.82 1.53 1.50 948.36 51 44 41 250 250 7 30 3 109 0.82 1.53 1.50 951.96 53 45 42 252 251 8 35 3 109 0.80 1.50 1.45 955.56 55 46 43 251 251 9 40 3 109 0.76 1.42 1.40 959.11 56 46 43 250 250 

10 45 3 110 0.76 1.42 1.40 962.60 58 48 44 242 250 11 50 3 109 0.72 1.35 1.30 966.10 59 48 44 250 250 12 55 3 109 0.72 1.35 1.30 969.51 60 50 43 253 249 13 60 3 110 0.67 1.25 1.24 972.92 60 50 44 255 251 14 65 3 109 0.67 1.25 1.24 976.29 60 52 44 250 250 15 70 3 109 0.67 1.25 1.25 979.66 61 52 44 248 249 16 75 3 110 0.67 1.25 1.25 983.04 61 53 45 252 250 17 80 3 110 0.65 1.21 1.20 986.40 61 53 45 256 248 18 85 3 110 0.63 1.18 1.20 989.74 61 54 45 249 251 19 90 3 109 0.62 1.16 1.15 993.06 61 54 44 255 248 20 95 3 109 0.62 1.16 1.15 996.26 62 55 45 245 250 21 100 2 108 0.57 1.07 1.07 999.45 62 55 44 255 248 22 105 2 106 0.56 1.05 1.05 1002.40 62 55 45 247 249 23 110 2 109 0.49 0.92 0.93 1005.56 62 55 45 250 250 24 115 2 109 0.49 0.92 0.93 1008.63 62 55 45 248 251 

120 10:06 1011.71

1 120 10:13 2 109 0.75 1.40 1.40 1011.71 60 56 46 246 251 2 125 2 109 0.75 1.40 1.40 1015.28 61 57 46 248 249 3 130 2 110 0.75 1.40 1.40 1018.80 61 57 45 250 253 4 135 3 110 0.76 1.42 1.45 1022.45 62 57 46 248 250 5 140 3 111 0.88 1.64 1.70 1026.05 65 58 46 251 251 6 145 3 112 0.87 1.63 1.70 1029.95 67 59 47 249 249 7 150 3 112 0.83 1.55 1.60 1033.86 69 59 48 250 248 8 155 3 113 0.81 1.51 1.55 1037.59 70 61 50 251 250 9 160 3 113 0.80 1.50 1.50 1041.45 72 62 51 257 250 

10 165 3 114 0.79 1.48 1.50 1045.08 73 63 52 248 249 11 170 3 114 0.75 1.40 1.45 1048.77 74 64 52 246 251 12 175 3 115 0.75 1.40 1.45 1052.34 75 65 53 250 250 13 180 3 115 0.69 1.29 1.35 1055.80 76 66 53 248 249 14 185 3 116 0.68 1.27 1.30 1059.52 77 67 55 252 252 15 190 3 116 0.74 1.39 1.45 1062.91 77 68 55 243 248 16 195 3 117 0.76 1.43 1.50 1066.48 78 69 55 241 251 17 200 3 117 0.79 1.48 1.50 1070.15 79 70 55 244 250 18 205 3 117 0.79 1.49 1.50 1073.81 79 71 55 248 252 19 210 3 118 0.81 1.52 1.60 1077.51 80 72 56 241 251 20 215 3 118 0.82 1.55 1.60 1081.28 80 72 55 243 251 21 220 3 119 0.80 1.51 1.60 1085.04 80 73 56 251 252 22 225 3 119 0.81 1.53 1.60 1088.82 81 73 56 242 246 23 230 3 119 0.79 1.49 1.55 1092.60 81 74 57 249 249 24 235 3 120 0.79 1.50 1.55 1096.39 81 74 57 248 244 

240 12:13 1100.17

Average 240 112.0 0.74 1.39 1.40 170.054 64.8 57.3 47.4 249.2 249.8 

61.00
Company JM McPherson

Source Designation 122 M1 DCTest Date 2/1/2012 Assumed Moisture (Bws) 2Test Number M5-29 R2 Condensate Volume (Vlc) 8.9Operator BC/PD Silica Gel Weight Gain (Vlc) 33.9Filter Number 11081874 Nozzle Diameter (in.) 0.219Barometric Pressure (Pb) 30.13 Leak Rate Initial 0.000 @ 15"Stack Static Pressure (Ps) -0.51 Leak Rate Final 0.000 @ 5"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 5'B Meter Corr. Factor (Y) 1.002Meter Number MB-5 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.55 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Exp

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature DG

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (cubi

1 0 13:02 3 124 0.80 1.50 1.50 100.35 72 72 65 250 250 1042 5 3 124 0.80 1.50 1.50 104.03 72 72 57 248 249 1073 10 3 125 0.81 1.52 1.50 107.81 73 72 48 241 249 114 15 3 125 0.81 1.53 1.50 111.51 73 72 46 254 251 115 20 3 125 0.82 1.55 1.50 115.29 74 73 45 243 250 1196 25 3 126 0.82 1.55 1.50 119.02 76 72 47 257 251 1227 30 3 126 0.80 1.51 1.50 122.74 77 72 47 250 250 128 35 3 126 0.80 1.51 1.50 126.43 77 72 46 251 248 1309 40 3 126 0.75 1.42 1.40 130.12 78 72 47 251 250 13

10 45 3 126 0.75 1.42 1.40 133.78 79 73 47 246 250 13711 50 3 127 0.69 1.31 1.30 137.36 79 73 48 246 250 14012 55 3 127 0.70 1.33 1.30 141.09 80 74 48 247 250 14413 60 3 128 0.74 1.41 1.40 144.55 82 74 49 242 250 1414 65 3 128 0.75 1.43 1.40 148.24 82 74 49 250 249 1515 70 3 128 0.76 1.45 1.45 151.90 81 75 48 251 251 1516 75 3 129 0.76 1.45 1.45 155.54 82 76 49 250 249 15917 80 3 129 0.78 1.49 1.50 159.19 82 76 48 243 251 16218 85 3 129 0.78 1.49 1.50 162.85 82 76 48 250 250 1619 90 3 129 0.84 1.61 1.60 166.61 83 76 50 248 250 17020 95 3 129 0.84 1.61 1.60 170.42 83 77 51 246 250 17421 100 3 129 0.78 1.50 1.50 174.23 84 77 52 241 250 17722 105 3 129 0.78 1.50 1.50 177.90 84 77 52 250 250 1823 110 3 129 0.78 1.50 1.50 181.57 84 77 51 248 249 1824 115 3 129 0.78 1.50 1.50 185.50 84 77 51 249 250 189

120 15:03 189.16

1 120 15:07 3 129 0.80 1.55 1.50 189.16 80 79 60 250 250 1922 125 3 131 0.80 1.55 1.50 192.83 83 79 54 250 249 193 130 3 131 0.80 1.55 1.55 196.55 83 79 52 249 251 2004 135 3 132 0.78 1.51 1.50 200.27 84 79 53 249 249 205 140 3 132 0.80 1.55 1.55 203.97 84 79 53 250 251 2076 145 3 132 0.80 1.55 1.55 207.67 84 79 53 250 250 217 150 3 132 0.80 1.56 1.55 211.39 84 79 55 248 249 218 155 3 131 0.80 1.56 1.55 215.10 84 79 55 250 250 219 160 3 131 0.75 1.46 1.45 218.79 84 79 55 255 251 222

10 165 3 131 0.75 1.46 1.45 222.47 84 79 54 251 248 2211 170 3 131 0.68 1.33 1.30 226.14 84 79 53 250 250 22912 175 3 131 0.68 1.33 1.30 229.78 84 79 55 250 250 2313 180 3 131 0.66 1.29 1.30 233.31 84 79 55 250 250 2314 185 3 131 0.66 1.29 1.30 236.71 84 79 55 247 251 24015 190 3 132 0.62 1.22 1.20 240.39 84 79 56 252 250 2416 195 3 132 0.62 1.22 1.20 243.77 84 79 56 250 250 24717 200 3 132 0.62 1.22 1.20 247.03 84 79 56 251 252 25018 205 3 132 0.62 1.22 1.20 250.32 84 79 56 250 250 2519 210 3 132 0.59 1.16 1.15 253.57 84 79 58 246 249 2520 215 3 132 0.59 1.16 1.15 256.79 84 79 58 250 250 25921 220 3 132 0.59 1.17 1.15 260.07 84 79 58 253 251 2622 225 3 132 0.59 1.17 1.15 263.26 84 79 58 250 250 2623 230 3 132 0.59 1.17 1.15 266.57 84 79 58 250 250 26924 235 3 132 0.59 1.17 1.15 269.76 84 79 58 250 250 272

240 17:07 273.07

Average 240 129.3 0.74 1.42 1.40 172.716 82 77 53 249 250 1

79.06
Company JM McPherson

Source Designation 122 M1 DCTest Date 2/2/2012 Assumed Moisture (Bws) 2Test Number M5-29 R3 Condensate Volume (Vlc) 25.7Operator BC/PD Silica Gel Weight Gain (Vlc) 29.5Filter Number 11081877 Nozzle Diameter (in.) 0.219Barometric Pressure (Pb) 30.21 Leak Rate Initial 0.000 @ 10"Stack Static Pressure (Ps) -0.51 Leak Rate Final 0.000 @ 10"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 5'B Meter Corr. Factor (Y) 1.002Meter Number MB-5 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.55 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Exp

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature DG

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (cubi

1 0 7:35 3 114 0.79 1.46 1.40 273.55 41 41 40 248 248 2772 5 3 114 0.79 1.46 1.40 277.07 42 41 36 248 230 2803 10 3 114 0.79 1.46 1.40 280.58 44 42 37 248 236 2844 15 3 114 0.79 1.46 1.40 284.04 47 42 38 249 250 2875 20 3 114 0.81 1.50 1.45 287.44 49 43 38 248 249 2906 25 3 115 0.81 1.50 1.45 290.91 51 44 39 250 250 2947 30 3 115 0.79 1.46 1.40 294.43 52 44 39 249 251 2978 35 3 115 0.79 1.46 1.40 297.95 54 45 40 250 250 309 40 3 116 0.74 1.37 1.35 301.47 55 46 40 250 250 304

10 45 3 116 0.74 1.37 1.35 305.02 56 46 42 250 250 3011 50 3 116 0.70 1.29 1.30 308.24 56 47 41 248 249 3112 55 3 116 0.70 1.29 1.30 311.30 56 47 41 250 250 31413 60 3 116 0.64 1.18 1.15 314.66 57 48 42 249 250 31714 65 3 116 0.64 1.18 1.15 317.89 57 48 42 250 250 3215 70 3 116 0.64 1.18 1.15 321.12 59 50 42 250 249 32416 75 3 116 0.64 1.18 1.15 324.33 59 50 42 250 250 32717 80 3 116 0.64 1.18 1.15 327.56 59 51 44 250 250 33018 85 3 115 0.59 1.09 1.10 330.76 59 51 44 250 250 3319 90 3 112 0.54 1.00 1.00 333.84 60 52 43 250 250 3320 95 3 112 0.54 1.00 1.00 336.80 60 52 43 250 250 33921 100 3 110 0.55 1.02 1.00 340.00 61 53 44 248 253 3422 105 3 110 0.55 1.02 1.00 343.00 61 53 44 250 250 3423 110 3 110 0.55 1.02 1.00 346.03 61 53 44 250 250 34924 115 3 110 0.55 1.02 1.00 349.03 61 53 44 250 250 352

120 9:35 352.03

1 120 9:42 3 113 0.77 1.42 1.45 352.03 56 54 50 246 248 352 125 3 113 0.77 1.42 1.45 355.70 59 54 46 249 251 3593 130 3 113 0.79 1.46 1.50 359.30 60 55 47 252 250 3624 135 3 113 0.79 1.46 1.50 363.00 62 55 46 250 250 365 140 3 114 0.81 1.50 1.50 366.59 63 56 48 250 250 3706 145 3 114 0.81 1.50 1.50 370.44 65 56 48 250 250 3747 150 3 114 0.82 1.51 1.60 374.04 65 56 48 240 249 3778 155 3 114 0.79 1.46 1.50 377.81 66 57 49 255 250 389 160 3 114 0.72 1.33 1.40 381.47 66 57 49 250 250 384

10 165 3 114 0.69 1.27 1.30 384.98 66 59 49 250 250 3811 170 3 114 0.69 1.27 1.30 388.36 66 60 50 250 250 3912 175 3 114 0.70 1.29 1.40 391.80 67 60 50 250 250 3913 180 3 114 0.72 1.33 1.40 395.35 67 60 50 250 250 3914 185 3 114 0.72 1.33 1.40 398.81 67 60 50 250 250 40215 190 3 114 0.75 1.39 1.40 402.30 67 60 50 248 251 4016 195 3 114 0.75 1.39 1.40 405.70 67 60 50 250 250 40917 200 3 114 0.77 1.43 1.50 409.23 67 61 49 251 251 41218 205 3 114 0.77 1.43 1.50 412.87 68 61 50 243 251 4119 210 3 114 0.82 1.53 1.60 416.63 68 61 50 250 250 42020 215 3 114 0.82 1.53 1.60 420.38 68 61 50 246 249 42421 220 3 114 0.82 1.53 1.60 424.08 68 61 50 250 250 42722 225 3 114 0.82 1.53 1.60 427.87 68 61 50 250 250 4323 230 3 114 0.82 1.53 1.60 431.57 68 61 50 249 250 4324 235 3 114 0.82 1.53 1.60 435.27 68 61 50 250 250 43

240 11:42 438.96

Average 240 114.0 0.73 1.34 1.36 165.415 60.2 53.1 45.2 249.3 249.3 35

56.65
Company JM McPherson

Source Designation 122 M1 DCTest Date 2/1/2012 Assumed Moisture (Bws) 2

Test Number 1 Condensate Volume (Vlc) 19.2Operator JP Silica Gel Weight Gain (Vlc) 29.5Filter Number NA Nozzle Diameter (in.) 0.217Barometric Pressure (Pb) 30.13 Leak Rate Initial .002 @12"Stack Static Pressure (Pg) -0.51 Leak Rate Final .006 @ 6"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84Pitot Tube Number 5 ft C Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0Delta ∆H@ 1.72 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Actual Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box E

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperatu

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 8:06 3.5 107 0.64 1.29 1.23 73.88 37 37 34 NA NA NA 2 5 3.5 106 0.64 1.29 1.23 76.94 38 37 34 NA NA NA 3 10 3.5 108 0.65 1.31 1.25 80.00 41 38 33 NA NA NA 4 15 3.5 108 0.65 1.31 1.25 83.07 43 38 34 NA NA NA 5 20 3.5 108 0.72 1.45 1.39 86.16 46 38 34 NA NA NA 6 25 3.5 108 0.72 1.45 1.40 89.42 49 40 34 NA NA NA 7 30 3.5 107 0.73 1.47 1.42 92.69 51 41 33 NA NA NA 8 35 3.5 107 0.73 1.47 1.42 96.00 53 42 34 NA NA NA 9 40 3.5 107 0.71 1.43 1.39 99.31 55 43 34 NA NA NA 

10 45 3.5 107 0.71 1.43 1.39 102.63 57 45 34 NA NA NA 11 50 3.5 107 0.68 1.37 1.34 105.92 58 46 34 NA NA NA 12 55 3.5 107 0.68 1.37 1.34 109.16 59 47 34 NA NA NA 13 60 3.5 107 0.64 1.29 1.27 112.44 59 48 34 NA NA NA 14 65 3.5 107 0.64 1.29 1.27 115.61 60 49 34 NA NA NA 15 70 3.5 107 0.69 1.39 1.37 118.76 60 50 35 NA NA NA 16 75 3.5 107 0.69 1.39 1.37 122.03 60 50 35 NA NA NA 17 80 4 108 0.78 1.57 1.56 125.32 61 51 35 NA NA NA 18 85 4 108 0.78 1.57 1.56 128.83 62 52 35 NA NA NA 19 90 4 108 0.82 1.65 1.64 132.32 63 53 36 NA NA NA 20 95 4 108 0.82 1.65 1.65 135.91 63 53 36 NA NA NA 21 100 4 108 0.83 1.67 1.67 139.51 64 54 36 NA NA NA 22 105 4 108 0.84 1.69 1.69 143.11 64 54 37 NA NA NA 23 110 4 108 0.79 1.59 1.60 146.75 65 55 37 NA NA NA 24 115 4 107 0.79 1.59 1.60 150.30 65 55 37 NA NA NA 

120 10:06 153.83

1 120 10:13 3.5 107 0.69 1.39 1.40 153.83 57 56 42 NA NA NA 2 125 3.5 107 0.69 1.39 1.40 157.15 63 56 38 NA NA NA 3 130 3.5 106 0.72 1.45 1.47 160.48 64 57 38 NA NA NA 4 135 3.5 106 0.72 1.45 1.47 163.84 65 57 38 NA NA NA 5 140 3.5 107 0.73 1.47 1.49 167.25 67 58 39 NA NA NA 6 145 3.5 107 0.73 1.47 1.50 170.65 69 59 40 NA NA NA 7 150 4 108 0.75 1.51 1.54 174.09 71 60 40 NA NA NA 8 155 4 108 0.75 1.51 1.54 177.57 72 61 40 NA NA NA 9 160 4 109 0.72 1.45 1.49 181.06 74 63 40 NA NA NA 

10 165 4 109 0.72 1.45 1.49 184.53 76 64 41 NA NA NA 11 170 3.5 109 0.65 1.31 1.34 187.96 77 66 41 NA NA NA 12 175 3.5 109 0.65 1.31 1.35 191.26 78 67 42 NA NA NA 13 180 3.5 111 0.60 1.21 1.25 194.53 78 68 42 NA NA NA 14 185 3.5 111 0.60 1.21 1.26 197.72 79 69 42 NA NA NA 15 190 3.5 112 0.57 1.15 1.20 200.90 80 70 42 NA NA NA 16 195 3.5 112 0.57 1.15 1.19 204.00 80 71 43 NA NA NA 17 200 3 113 0.55 1.11 1.15 207.09 80 72 42 NA NA NA 18 205 3 113 0.55 1.11 1.15 210.15 81 72 43 NA NA NA 19 210 3 113 0.56 1.13 1.18 213.16 81 73 44 NA NA NA 20 215 3 113 0.56 1.13 1.18 216.26 81 74 44 NA NA NA 21 220 3 114 0.53 1.08 1.12 219.32 81 74 44 NA NA NA 22 225 3 114 0.53 1.08 1.12 222.33 81 75 44 NA NA NA 23 230 3 114 0.52 1.06 1.10 225.35 81 75 44 NA NA NA 24 235 3 114 0.52 1.06 1.10 228.33 82 75 44 NA NA NA 

240 12:13 231.31

Average 240 108.8 0.68 1.36 1.37 157.430 65.2 56.4 38.1 #DIV/0! #DIV/0! #DIV/0! 

60.82
Company JM McPherson

Source Designation Line 122 M1DCTest Date 2/1/2012 Assumed Moisture (Bws) 2Test Number 2 Condensate Volume (Vlc) 18.1Operator JP Silica Gel Weight Gain (Vlc) 41.5Filter Number NA Nozzle Diameter (in.) 0.217Barometric Pressure (Pb) 30.13 Leak Rate Initial .000 @ 12"Stack Static Pressure (Ps) -0.51 Leak Rate Final .000 @ 7"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 5 ft C Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.72 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box Exit 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 13:02 2.5 109 0.51 1.03 1.05 231.61 75 75 56 NA NA NA 2 5 2.5 110 0.51 1.03 1.05 234.51 75 75 46 NA NA NA 3 10 2.5 116 0.54 1.09 1.11 237.41 75 74 44 NA NA NA 4 15 2.5 117 0.54 1.10 1.11 240.41 76 74 44 NA NA NA 5 20 2.5 120 0.58 1.18 1.19 243.40 77 74 44 NA NA NA 6 25 2.5 121 0.58 1.18 1.19 246.48 78 74 44 NA NA NA 7 30 2.5 121 0.60 1.22 1.23 249.60 78 74 44 NA NA NA 8 35 2.5 121 0.60 1.22 1.23 252.75 79 74 45 NA NA NA 9 40 2.5 122 0.63 1.29 1.29 255.89 79 73 45 NA NA NA 

10 45 2.5 122 0.63 1.29 1.29 259.08 80 74 46 NA NA NA 11 50 2.5 123 0.62 1.27 1.28 262.34 81 74 46 NA NA NA 12 55 2.5 123 0.62 1.27 1.28 265.53 81 74 47 NA NA NA 13 60 3 123 0.68 1.39 1.40 268.71 81 74 49 NA NA NA 14 65 3 123 0.68 1.40 1.40 272.06 82 75 49 NA NA NA 15 70 3 124 0.73 1.50 1.51 275.40 82 75 50 NA NA NA 16 75 3 124 0.73 1.50 1.51 278.88 82 75 50 NA NA NA 17 80 3 125 0.75 1.55 1.55 282.37 82 75 50 NA NA NA 18 85 3 125 0.75 1.55 1.55 285.91 82 75 50 NA NA NA 19 90 3 125 0.76 1.57 1.59 289.42 83 75 52 NA NA NA 20 95 3 125 0.76 1.57 1.59 292.97 83 75 51 NA NA NA 21 100 3 125 0.75 1.55 1.56 296.52 83 76 53 NA NA NA 22 105 3 125 0.75 1.55 1.56 300.04 83 76 53 NA NA NA 23 110 3 125 0.73 1.51 1.52 303.59 83 76 53 NA NA NA 24 115 3 125 0.73 1.52 1.52 307.09 83 76 52 NA NA NA 

120 15:02 310.55

1 120 15:07 3.5 126 0.81 1.69 1.69 310.55 78 76 60 NA NA NA 2 125 3.5 126 0.81 1.69 1.69 314.18 82 76 55 NA NA NA 3 130 3.5 127 0.82 1.71 1.71 317.83 83 76 52 NA NA NA 4 135 3.5 127 0.82 1.71 1.72 321.52 84 76 51 NA NA NA 5 140 3.5 128 0.78 1.63 1.63 325.22 84 77 52 NA NA NA 6 145 3.5 128 0.78 1.63 1.63 328.80 84 77 53 NA NA NA 7 150 3.5 127 0.77 1.61 1.62 332.41 84 77 52 NA NA NA 8 155 3.5 127 0.77 1.62 1.62 336.03 84 77 53 NA NA NA 9 160 3.5 127 0.76 1.60 1.60 339.59 84 77 53 NA NA NA 

10 165 3.5 127 0.76 1.60 1.60 343.12 84 77 53 NA NA NA 11 170 3 127 0.71 1.49 1.50 346.68 84 76 53 NA NA NA 12 175 3 127 0.71 1.50 1.50 350.13 84 76 53 NA NA NA 13 180 3 127 0.69 1.46 1.46 353.55 83 76 54 NA NA NA 14 185 3 127 0.69 1.46 1.46 356.91 83 76 54 NA NA NA 15 190 3 127 0.72 1.52 1.52 360.27 83 76 54 NA NA NA 16 195 3 127 0.72 1.52 1.52 363.69 83 76 54 NA NA NA 17 200 3.5 127 0.80 1.70 1.70 367.13 83 76 55 NA NA NA 18 205 3.5 127 0.80 1.70 1.70 370.79 83 75 55 NA NA NA 19 210 3.5 127 0.82 1.74 1.74 374.41 83 75 55 NA NA NA 20 215 3.5 127 0.82 1.74 1.74 378.08 84 76 56 NA NA NA 21 220 3.5 128 0.79 1.68 1.68 381.75 84 76 57 NA NA NA 22 225 3.5 128 0.79 1.68 1.68 385.40 83 76 57 NA NA NA 23 230 3.5 128 0.75 1.60 1.60 389.00 83 76 57 NA NA NA 24 235 3.5 128 0.75 1.60 1.60 392.50 83 76 58 NA NA NA 

240 17:07 396.01

Average 240 124.4 0.71 1.48 1.49 164.400 82 75 51 #DIV/0! #DIV/0! #DIV/0! 

78.54
Company JM McPherson

Source Designation Line 122 M1DCTest Date 2/2/2012 Assumed Moisture (Bws) 2Test Number 3 Condensate Volume (Vlc) 6.4Operator JP Silica Gel Weight Gain (Vlc) 26.8Filter Number NA Nozzle Diameter (in.) 0.217Barometric Pressure (Pb) 30.21 Leak Rate Initial .000 @ 15"Stack Static Pressure (Ps) -0.51 Leak Rate Final .000 @ 5"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 5 ft C Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.72 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box Exit 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 7:35 3.5 111 0.72 1.42 1.38 396.12 37 37 36 NA NA NA 2 5 3.5 111 0.72 1.42 1.38 399.32 41 38 34 NA NA NA 3 10 3.5 111 0.74 1.46 1.42 402.59 45 39 34 NA NA NA 4 15 3.5 111 0.74 1.46 1.42 405.88 47 39 34 NA NA NA 5 20 3.5 111 0.75 1.48 1.45 409.16 48 40 34 NA NA NA 6 25 3.5 112 0.75 1.48 1.45 412.49 50 40 34 NA NA NA 7 30 3.5 112 0.71 1.40 1.38 415.83 51 41 35 NA NA NA 8 35 3.5 112 0.71 1.40 1.38 419.07 52 42 35 NA NA NA 9 40 3.5 113 0.70 1.38 1.36 422.33 52 42 35 NA NA NA 

10 45 3.5 113 0.70 1.38 1.36 425.57 53 43 35 NA NA NA 11 50 3 113 0.65 1.28 1.27 428.82 54 44 35 NA NA NA 12 55 3 113 0.65 1.28 1.27 431.96 54 44 35 NA NA NA 13 60 3 113 0.63 1.25 1.24 435.10 54 45 36 NA NA NA 14 65 3 113 0.63 1.25 1.24 438.20 55 45 36 NA NA NA 15 70 3.5 112 0.69 1.36 1.36 441.27 55 46 37 NA NA NA 16 75 3.5 112 0.69 1.36 1.36 444.48 55 46 37 NA NA NA 17 80 3.5 111 0.76 1.50 1.50 447.70 56 47 37 NA NA NA 18 85 3.5 111 0.76 1.50 1.50 451.12 57 47 37 NA NA NA 19 90 4 110 0.79 1.56 1.57 454.53 57 48 38 NA NA NA 20 95 4 110 0.79 1.56 1.57 458.00 58 49 39 NA NA NA 21 100 4 110 0.80 1.58 1.59 461.47 58 49 39 NA NA NA 22 105 4 110 0.80 1.58 1.59 465.00 58 49 39 NA NA NA 23 110 4 109 0.78 1.54 1.56 468.52 58 49 39 NA NA NA 24 115 4 109 0.78 1.54 1.56 472.01 58 49 39 NA NA NA 

120 9:35 475.50

1 120 9:42 3 108 0.56 1.11 1.12 475.50 51 50 45 NA NA NA 2 125 3 108 0.56 1.11 1.12 478.40 57 51 41 NA NA NA 3 130 3 109 0.55 1.09 1.11 481.34 59 51 40 NA NA NA 4 135 3 109 0.55 1.09 1.11 484.29 60 52 40 NA NA NA 5 140 3 110 0.58 1.15 1.17 487.20 61 53 41 NA NA NA 6 145 3 110 0.58 1.15 1.17 490.18 63 54 41 NA NA NA 7 150 3 110 0.60 1.19 1.22 493.22 63 54 42 NA NA NA 8 155 3 110 0.60 1.19 1.22 496.31 64 55 42 NA NA NA 9 160 3 110 0.60 1.19 1.22 499.40 64 55 42 NA NA NA 

10 165 3 110 0.60 1.19 1.22 502.48 63 56 42 NA NA NA 11 170 3 110 0.59 1.17 1.21 505.56 64 56 43 NA NA NA 12 175 3 110 0.59 1.17 1.21 508.60 64 56 43 NA NA NA 13 180 3.5 110 0.64 1.26 1.31 511.68 64 57 44 NA NA NA 14 185 3.5 110 0.64 1.27 1.31 514.87 64 57 44 NA NA NA 15 190 3.5 110 0.69 1.37 1.42 518.02 64 57 45 NA NA NA 16 195 3.5 110 0.69 1.37 1.42 521.34 64 57 44 NA NA NA 17 200 3.5 109 0.73 1.45 1.51 524.68 65 57 44 NA NA NA 18 205 3.5 109 0.73 1.45 1.51 528.07 65 57 44 NA NA NA 19 210 3.5 110 0.74 1.47 1.53 531.51 65 57 45 NA NA NA 20 215 3.5 110 0.74 1.47 1.53 534.95 65 57 45 NA NA NA 21 220 3.5 110 0.70 1.40 1.45 538.40 64 57 45 NA NA NA 22 225 3.5 110 0.70 1.40 1.45 541.76 64 57 45 NA NA NA 23 230 3.5 110 0.68 1.36 1.42 545.10 64 57 45 NA NA NA 24 235 3.5 110 0.68 1.36 1.42 548.40 64 57 45 NA NA NA 

240 11:42 551.70

Average 240 110.5 0.68 1.35 1.37 155.582 57.7 49.7 39.7 #DIV/0! #DIV/0! #DIV/0! 

53.68
Company JM McPherson

Source Designation 122 M1 DCTest Date 2/1/2012 Assumed Moisture (Bws) 2

Test Number 1 Condensate Volume (Vlc) 19.2Operator JP Silica Gel Weight Gain (Vlc) 29.5Filter Number NA Nozzle Diameter (in.) 0.217Barometric Pressure (Pb) 30.13 Leak Rate Initial .002 @12"Stack Static Pressure (Pg) -0.51 Leak Rate Final .006 @ 6"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84Pitot Tube Number 5 ft C Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0Delta ∆H@ 1.72 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Actual Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box E

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperatu

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 8:06 3.5 107 0.64 1.29 1.23 73.88 37 37 34 NA NA NA 2 5 3.5 106 0.64 1.29 1.23 76.94 38 37 34 NA NA NA 3 10 3.5 108 0.65 1.31 1.25 80.00 41 38 33 NA NA NA 4 15 3.5 108 0.65 1.31 1.25 83.07 43 38 34 NA NA NA 5 20 3.5 108 0.72 1.45 1.39 86.16 46 38 34 NA NA NA 6 25 3.5 108 0.72 1.45 1.40 89.42 49 40 34 NA NA NA 7 30 3.5 107 0.73 1.47 1.42 92.69 51 41 33 NA NA NA 8 35 3.5 107 0.73 1.47 1.42 96.00 53 42 34 NA NA NA 9 40 3.5 107 0.71 1.43 1.39 99.31 55 43 34 NA NA NA 

10 45 3.5 107 0.71 1.43 1.39 102.63 57 45 34 NA NA NA 11 50 3.5 107 0.68 1.37 1.34 105.92 58 46 34 NA NA NA 12 55 3.5 107 0.68 1.37 1.34 109.16 59 47 34 NA NA NA 13 60 3.5 107 0.64 1.29 1.27 112.44 59 48 34 NA NA NA 14 65 3.5 107 0.64 1.29 1.27 115.61 60 49 34 NA NA NA 15 70 3.5 107 0.69 1.39 1.37 118.76 60 50 35 NA NA NA 16 75 3.5 107 0.69 1.39 1.37 122.03 60 50 35 NA NA NA 17 80 4 108 0.78 1.57 1.56 125.32 61 51 35 NA NA NA 18 85 4 108 0.78 1.57 1.56 128.83 62 52 35 NA NA NA 19 90 4 108 0.82 1.65 1.64 132.32 63 53 36 NA NA NA 20 95 4 108 0.82 1.65 1.65 135.91 63 53 36 NA NA NA 21 100 4 108 0.83 1.67 1.67 139.51 64 54 36 NA NA NA 22 105 4 108 0.84 1.69 1.69 143.11 64 54 37 NA NA NA 23 110 4 108 0.79 1.59 1.60 146.75 65 55 37 NA NA NA 24 115 4 107 0.79 1.59 1.60 150.30 65 55 37 NA NA NA 

120 10:06 153.83

1 120 10:13 3.5 107 0.69 1.39 1.40 153.83 57 56 42 NA NA NA 2 125 3.5 107 0.69 1.39 1.40 157.15 63 56 38 NA NA NA 3 130 3.5 106 0.72 1.45 1.47 160.48 64 57 38 NA NA NA 4 135 3.5 106 0.72 1.45 1.47 163.84 65 57 38 NA NA NA 5 140 3.5 107 0.73 1.47 1.49 167.25 67 58 39 NA NA NA 6 145 3.5 107 0.73 1.47 1.50 170.65 69 59 40 NA NA NA 7 150 4 108 0.75 1.51 1.54 174.09 71 60 40 NA NA NA 8 155 4 108 0.75 1.51 1.54 177.57 72 61 40 NA NA NA 9 160 4 109 0.72 1.45 1.49 181.06 74 63 40 NA NA NA 

10 165 4 109 0.72 1.45 1.49 184.53 76 64 41 NA NA NA 11 170 3.5 109 0.65 1.31 1.34 187.96 77 66 41 NA NA NA 12 175 3.5 109 0.65 1.31 1.35 191.26 78 67 42 NA NA NA 13 180 3.5 111 0.60 1.21 1.25 194.53 78 68 42 NA NA NA 14 185 3.5 111 0.60 1.21 1.26 197.72 79 69 42 NA NA NA 15 190 3.5 112 0.57 1.15 1.20 200.90 80 70 42 NA NA NA 16 195 3.5 112 0.57 1.15 1.19 204.00 80 71 43 NA NA NA 17 200 3 113 0.55 1.11 1.15 207.09 80 72 42 NA NA NA 18 205 3 113 0.55 1.11 1.15 210.15 81 72 43 NA NA NA 19 210 3 113 0.56 1.13 1.18 213.16 81 73 44 NA NA NA 20 215 3 113 0.56 1.13 1.18 216.26 81 74 44 NA NA NA 21 220 3 114 0.53 1.08 1.12 219.32 81 74 44 NA NA NA 22 225 3 114 0.53 1.08 1.12 222.33 81 75 44 NA NA NA 23 230 3 114 0.52 1.06 1.10 225.35 81 75 44 NA NA NA 24 235 3 114 0.52 1.06 1.10 228.33 82 75 44 NA NA NA 

240 12:13 231.31

Average 240 108.8 0.68 1.36 1.37 157.430 65.2 56.4 38.1 #DIV/0! #DIV/0! #DIV/0! 

60.82
Company JM McPherson

Source Designation Line 122 M1DCTest Date 2/1/2012 Assumed Moisture (Bws) 2Test Number 2 Condensate Volume (Vlc) 18.1Operator JP Silica Gel Weight Gain (Vlc) 41.5Filter Number NA Nozzle Diameter (in.) 0.217Barometric Pressure (Pb) 30.13 Leak Rate Initial .000 @ 12"Stack Static Pressure (Ps) -0.51 Leak Rate Final .000 @ 7"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 5 ft C Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.72 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box Exit 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 13:02 2.5 109 0.51 1.03 1.05 231.61 75 75 56 NA NA NA 2 5 2.5 110 0.51 1.03 1.05 234.51 75 75 46 NA NA NA 3 10 2.5 116 0.54 1.09 1.11 237.41 75 74 44 NA NA NA 4 15 2.5 117 0.54 1.10 1.11 240.41 76 74 44 NA NA NA 5 20 2.5 120 0.58 1.18 1.19 243.40 77 74 44 NA NA NA 6 25 2.5 121 0.58 1.18 1.19 246.48 78 74 44 NA NA NA 7 30 2.5 121 0.60 1.22 1.23 249.60 78 74 44 NA NA NA 8 35 2.5 121 0.60 1.22 1.23 252.75 79 74 45 NA NA NA 9 40 2.5 122 0.63 1.29 1.29 255.89 79 73 45 NA NA NA 

10 45 2.5 122 0.63 1.29 1.29 259.08 80 74 46 NA NA NA 11 50 2.5 123 0.62 1.27 1.28 262.34 81 74 46 NA NA NA 12 55 2.5 123 0.62 1.27 1.28 265.53 81 74 47 NA NA NA 13 60 3 123 0.68 1.39 1.40 268.71 81 74 49 NA NA NA 14 65 3 123 0.68 1.40 1.40 272.06 82 75 49 NA NA NA 15 70 3 124 0.73 1.50 1.51 275.40 82 75 50 NA NA NA 16 75 3 124 0.73 1.50 1.51 278.88 82 75 50 NA NA NA 17 80 3 125 0.75 1.55 1.55 282.37 82 75 50 NA NA NA 18 85 3 125 0.75 1.55 1.55 285.91 82 75 50 NA NA NA 19 90 3 125 0.76 1.57 1.59 289.42 83 75 52 NA NA NA 20 95 3 125 0.76 1.57 1.59 292.97 83 75 51 NA NA NA 21 100 3 125 0.75 1.55 1.56 296.52 83 76 53 NA NA NA 22 105 3 125 0.75 1.55 1.56 300.04 83 76 53 NA NA NA 23 110 3 125 0.73 1.51 1.52 303.59 83 76 53 NA NA NA 24 115 3 125 0.73 1.52 1.52 307.09 83 76 52 NA NA NA 

120 15:02 310.55

1 120 15:07 3.5 126 0.81 1.69 1.69 310.55 78 76 60 NA NA NA 2 125 3.5 126 0.81 1.69 1.69 314.18 82 76 55 NA NA NA 3 130 3.5 127 0.82 1.71 1.71 317.83 83 76 52 NA NA NA 4 135 3.5 127 0.82 1.71 1.72 321.52 84 76 51 NA NA NA 5 140 3.5 128 0.78 1.63 1.63 325.22 84 77 52 NA NA NA 6 145 3.5 128 0.78 1.63 1.63 328.80 84 77 53 NA NA NA 7 150 3.5 127 0.77 1.61 1.62 332.41 84 77 52 NA NA NA 8 155 3.5 127 0.77 1.62 1.62 336.03 84 77 53 NA NA NA 9 160 3.5 127 0.76 1.60 1.60 339.59 84 77 53 NA NA NA 

10 165 3.5 127 0.76 1.60 1.60 343.12 84 77 53 NA NA NA 11 170 3 127 0.71 1.49 1.50 346.68 84 76 53 NA NA NA 12 175 3 127 0.71 1.50 1.50 350.13 84 76 53 NA NA NA 13 180 3 127 0.69 1.46 1.46 353.55 83 76 54 NA NA NA 14 185 3 127 0.69 1.46 1.46 356.91 83 76 54 NA NA NA 15 190 3 127 0.72 1.52 1.52 360.27 83 76 54 NA NA NA 16 195 3 127 0.72 1.52 1.52 363.69 83 76 54 NA NA NA 17 200 3.5 127 0.80 1.70 1.70 367.13 83 76 55 NA NA NA 18 205 3.5 127 0.80 1.70 1.70 370.79 83 75 55 NA NA NA 19 210 3.5 127 0.82 1.74 1.74 374.41 83 75 55 NA NA NA 20 215 3.5 127 0.82 1.74 1.74 378.08 84 76 56 NA NA NA 21 220 3.5 128 0.79 1.68 1.68 381.75 84 76 57 NA NA NA 22 225 3.5 128 0.79 1.68 1.68 385.40 83 76 57 NA NA NA 23 230 3.5 128 0.75 1.60 1.60 389.00 83 76 57 NA NA NA 24 235 3.5 128 0.75 1.60 1.60 392.50 83 76 58 NA NA NA 

240 17:07 396.01

Average 240 124.4 0.71 1.48 1.49 164.400 82 75 51 #DIV/0! #DIV/0! #DIV/0! 

78.54
Company JM McPherson

Source Designation Line 122 M1DCTest Date 2/2/2012 Assumed Moisture (Bws) 2Test Number 3 Condensate Volume (Vlc) 6.4Operator JP Silica Gel Weight Gain (Vlc) 26.8Filter Number NA Nozzle Diameter (in.) 0.217Barometric Pressure (Pb) 30.21 Leak Rate Initial .000 @ 15"Stack Static Pressure (Ps) -0.51 Leak Rate Final .000 @ 5"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 5 ft C Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.72 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box Exit 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 7:35 3.5 111 0.72 1.42 1.38 396.12 37 37 36 NA NA NA 2 5 3.5 111 0.72 1.42 1.38 399.32 41 38 34 NA NA NA 3 10 3.5 111 0.74 1.46 1.42 402.59 45 39 34 NA NA NA 4 15 3.5 111 0.74 1.46 1.42 405.88 47 39 34 NA NA NA 5 20 3.5 111 0.75 1.48 1.45 409.16 48 40 34 NA NA NA 6 25 3.5 112 0.75 1.48 1.45 412.49 50 40 34 NA NA NA 7 30 3.5 112 0.71 1.40 1.38 415.83 51 41 35 NA NA NA 8 35 3.5 112 0.71 1.40 1.38 419.07 52 42 35 NA NA NA 9 40 3.5 113 0.70 1.38 1.36 422.33 52 42 35 NA NA NA 

10 45 3.5 113 0.70 1.38 1.36 425.57 53 43 35 NA NA NA 11 50 3 113 0.65 1.28 1.27 428.82 54 44 35 NA NA NA 12 55 3 113 0.65 1.28 1.27 431.96 54 44 35 NA NA NA 13 60 3 113 0.63 1.25 1.24 435.10 54 45 36 NA NA NA 14 65 3 113 0.63 1.25 1.24 438.20 55 45 36 NA NA NA 15 70 3.5 112 0.69 1.36 1.36 441.27 55 46 37 NA NA NA 16 75 3.5 112 0.69 1.36 1.36 444.48 55 46 37 NA NA NA 17 80 3.5 111 0.76 1.50 1.50 447.70 56 47 37 NA NA NA 18 85 3.5 111 0.76 1.50 1.50 451.12 57 47 37 NA NA NA 19 90 4 110 0.79 1.56 1.57 454.53 57 48 38 NA NA NA 20 95 4 110 0.79 1.56 1.57 458.00 58 49 39 NA NA NA 21 100 4 110 0.80 1.58 1.59 461.47 58 49 39 NA NA NA 22 105 4 110 0.80 1.58 1.59 465.00 58 49 39 NA NA NA 23 110 4 109 0.78 1.54 1.56 468.52 58 49 39 NA NA NA 24 115 4 109 0.78 1.54 1.56 472.01 58 49 39 NA NA NA 

120 9:35 475.50

1 120 9:42 3 108 0.56 1.11 1.12 475.50 51 50 45 NA NA NA 2 125 3 108 0.56 1.11 1.12 478.40 57 51 41 NA NA NA 3 130 3 109 0.55 1.09 1.11 481.34 59 51 40 NA NA NA 4 135 3 109 0.55 1.09 1.11 484.29 60 52 40 NA NA NA 5 140 3 110 0.58 1.15 1.17 487.20 61 53 41 NA NA NA 6 145 3 110 0.58 1.15 1.17 490.18 63 54 41 NA NA NA 7 150 3 110 0.60 1.19 1.22 493.22 63 54 42 NA NA NA 8 155 3 110 0.60 1.19 1.22 496.31 64 55 42 NA NA NA 9 160 3 110 0.60 1.19 1.22 499.40 64 55 42 NA NA NA 

10 165 3 110 0.60 1.19 1.22 502.48 63 56 42 NA NA NA 11 170 3 110 0.59 1.17 1.21 505.56 64 56 43 NA NA NA 12 175 3 110 0.59 1.17 1.21 508.60 64 56 43 NA NA NA 13 180 3.5 110 0.64 1.26 1.31 511.68 64 57 44 NA NA NA 14 185 3.5 110 0.64 1.27 1.31 514.87 64 57 44 NA NA NA 15 190 3.5 110 0.69 1.37 1.42 518.02 64 57 45 NA NA NA 16 195 3.5 110 0.69 1.37 1.42 521.34 64 57 44 NA NA NA 17 200 3.5 109 0.73 1.45 1.51 524.68 65 57 44 NA NA NA 18 205 3.5 109 0.73 1.45 1.51 528.07 65 57 44 NA NA NA 19 210 3.5 110 0.74 1.47 1.53 531.51 65 57 45 NA NA NA 20 215 3.5 110 0.74 1.47 1.53 534.95 65 57 45 NA NA NA 21 220 3.5 110 0.70 1.40 1.45 538.40 64 57 45 NA NA NA 22 225 3.5 110 0.70 1.40 1.45 541.76 64 57 45 NA NA NA 23 230 3.5 110 0.68 1.36 1.42 545.10 64 57 45 NA NA NA 24 235 3.5 110 0.68 1.36 1.42 548.40 64 57 45 NA NA NA 

240 11:42 551.70

Average 240 110.5 0.68 1.35 1.37 155.582 57.7 49.7 39.7 #DIV/0! #DIV/0! #DIV/0! 

53.68
Company JM Mcpherson

Source Designation M-2 dust collectorTest Date 2/1/2012 Assumed Moisture (Bws) 2

Test Number M0061 R1 Condensate Volume (Vlc) 18.4Operator MY Silica Gel Weight Gain (Vlc) 28.2Filter Number NA Nozzle Diameter (in.) 0.216Barometric Pressure (Pb) 30.13 Leak Rate Initial 0.00@15"Stack Static Pressure (Pg) -0.41 Leak Rate Final 0.00@6"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84Pitot Tube Number 4ftA Meter Corr. Factor (Y) 1.005Meter Number MB4 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0Delta ∆H@ 1.7 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Actual Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box E

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperatu

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 8:05 4 109 0.73 1.43 1.36 516.77 39 39 40 NA NA NA 2 5 4 109 0.73 1.43 1.36 520.14 40 40 37 NA NA NA 3 10 4 110 0.72 1.42 1.35 523.45 41 40 37 NA NA NA 4 15 4 110 0.72 1.42 1.35 526.70 41 40 38 NA NA NA 5 20 4 109 0.72 1.42 1.35 529.91 45 40 40 NA NA NA 6 25 4 109 0.73 1.43 1.37 533.12 47 41 41 NA NA NA 7 30 4 108 0.69 1.36 1.30 536.47 49 42 41 NA NA NA 8 35 4 108 0.69 1.36 1.30 539.74 50 43 42 NA NA NA 9 40 4 107 0.68 1.34 1.29 542.96 52 44 44 NA NA NA 

10 45 4 107 0.68 1.34 1.29 546.20 53 45 44 NA NA NA 11 50 4 106 0.66 1.30 1.26 549.39 54 45 44 NA NA NA 12 55 4 106 0.66 1.30 1.26 552.56 55 46 44 NA NA NA 13 60 4 105 0.62 1.22 1.19 555.72 55 47 44 NA NA NA 14 65 4 104 0.62 1.22 1.19 558.83 56 48 44 NA NA NA 15 70 4 104 0.68 1.34 1.31 561.94 57 49 44 NA NA NA 16 75 4 103 0.68 1.34 1.31 565.12 57 50 43 NA NA NA 17 80 4 102 0.71 1.40 1.37 568.35 58 50 44 NA NA NA 18 85 4 102 0.73 1.43 1.42 571.67 58 51 44 NA NA NA 19 90 4 101 0.75 1.47 1.46 574.97 58 52 44 NA NA NA 20 95 4 101 0.75 1.47 1.46 578.39 59 52 45 NA NA NA 21 100 4 101 0.73 1.43 1.43 581.84 59 53 45 NA NA NA 22 105 4 101 0.73 1.43 1.43 585.29 60 53 45 NA NA NA 23 110 4 101 0.74 1.45 1.45 588.74 61 54 45 NA NA NA 24 115 4 100 0.72 1.42 1.42 592.18 61 54 45 NA NA NA 

120 10:05 595.54

1 120 10:11 3 98 0.50 0.98 0.99 595.54 56 55 47 NA NA NA 2 125 3 99 0.50 0.98 0.99 598.54 60 56 45 NA NA NA 3 130 3 99 0.51 1.00 1.01 601.40 61 56 44 NA NA NA 4 135 3 99 0.50 0.98 0.99 604.34 62 56 45 NA NA NA 5 140 3 99 0.57 1.12 1.14 607.25 64 57 47 NA NA NA 6 145 3 100 0.60 1.18 1.20 610.28 66 58 48 NA NA NA 7 150 3 101 0.61 1.20 1.22 613.36 67 59 49 NA NA NA 8 155 3 101 0.61 1.20 1.22 616.54 69 60 49 NA NA NA 9 160 3 101 0.61 1.20 1.22 619.71 71 62 50 NA NA NA 

10 165 3 101 0.61 1.20 1.23 622.85 73 64 51 NA NA NA 11 170 3 102 0.62 1.22 1.25 626.01 74 65 51 NA NA NA 12 175 4 102 0.63 1.24 1.27 629.10 75 67 52 NA NA NA 13 180 4 103 0.58 1.14 1.18 632.29 76 68 52 NA NA NA 14 185 4 103 0.58 1.14 1.18 635.45 76 70 53 NA NA NA 15 190 4 103 0.63 1.24 1.28 638.58 78 71 54 NA NA NA 16 195 4 103 0.62 1.22 1.26 641.78 79 72 54 NA NA NA 17 200 4 103 0.63 1.24 1.29 645.04 80 73 53 NA NA NA 18 205 4 104 0.61 1.21 1.25 648.30 81 74 54 NA NA NA 19 210 4 104 0.61 1.21 1.25 651.56 82 76 54 NA NA NA 20 215 4 104 0.61 1.21 1.25 654.82 82 76 54 NA NA NA 21 220 4 105 0.59 1.17 1.21 658.07 82 77 54 NA NA NA 22 225 4 105 0.59 1.17 1.21 661.24 83 78 54 NA NA NA 23 230 4 105 0.59 1.17 1.22 664.43 83 78 55 NA NA NA 24 235 4 106 0.59 1.17 1.22 667.71 84 79 55 NA NA NA 

240 12:11 670.99

Average 240 103.6 0.65 1.27 1.27 154.223 63.1 56.8 46.8 #DIV/0! #DIV/0! #DIV/0! 

59.94
Company JM Mcpherson

Source Designation M-2 dust collectorTest Date 2/1/2012 Assumed Moisture (Bws) 2Test Number 2 Condensate Volume (Vlc) 13.6Operator MY Silica Gel Weight Gain (Vlc) 30.6Filter Number NA Nozzle Diameter (in.) 0.216Barometric Pressure (Pb) 30.13 Leak Rate Initial 0.005@15"Stack Static Pressure (Ps) -0.41 Leak Rate Final 0.000@6"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 4ftA Meter Corr. Factor (Y) 1.005Meter Number MB4 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.7 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box Exit 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 13:00 2 107 0.59 1.18 1.19 671.63 79 79 67 NA NA NA 2 5 2 109 0.57 1.14 1.15 674.70 79 78 65 NA NA NA 3 10 2 109 0.57 1.15 1.15 677.78 79 78 60 NA NA NA 4 15 2 110 0.57 1.15 1.15 680.88 80 78 55 NA NA NA 5 20 2 110 0.60 1.21 1.21 683.97 80 78 55 NA NA NA 6 25 2 109 0.60 1.21 1.22 687.10 80 77 53 NA NA NA 7 30 2 110 0.60 1.21 1.22 690.29 80 77 53 NA NA NA 8 35 2 110 0.60 1.21 1.22 693.46 80 77 54 NA NA NA 9 40 2 110 0.60 1.21 1.22 696.62 80 77 53 NA NA NA 

10 45 2 110 0.62 1.26 1.26 699.82 80 77 53 NA NA NA 11 50 2 111 0.61 1.24 1.24 702.99 80 77 53 NA NA NA 12 55 2 111 0.60 1.22 1.22 706.19 80 76 52 NA NA NA 13 60 2 111 0.61 1.24 1.24 709.36 79 76 52 NA NA NA 14 65 2 111 0.60 1.22 1.23 712.55 79 76 53 NA NA NA 15 70 2 111 0.62 1.26 1.27 715.72 78 76 53 NA NA NA 16 75 2 111 0.64 1.31 1.31 718.92 78 75 52 NA NA NA 17 80 2 111 0.64 1.31 1.31 722.15 78 75 52 NA NA NA 18 85 2 112 0.64 1.31 1.31 725.40 77 75 52 NA NA NA 19 90 2 112 0.64 1.31 1.31 728.67 77 75 52 NA NA NA 20 95 2 112 0.64 1.31 1.31 731.91 78 75 53 NA NA NA 21 100 2 112 0.63 1.29 1.29 735.12 79 75 53 NA NA NA 22 105 2 113 0.63 1.29 1.30 738.35 79 75 53 NA NA NA 23 110 2 113 0.63 1.30 1.30 741.59 79 75 53 NA NA NA 24 115 2 113 0.63 1.30 1.30 744.84 79 75 53 NA NA NA 

120 15:00 748.13

1 120 15:06 2 113 0.75 1.55 1.55 748.13 76 76 58 NA NA NA 2 125 2 114 0.77 1.59 1.59 751.73 78 75 56 NA NA NA 3 130 2 114 0.76 1.57 1.57 755.34 79 76 55 NA NA NA 4 135 2 114 0.76 1.57 1.57 758.95 80 76 55 NA NA NA 5 140 2 114 0.75 1.56 1.55 762.52 79 76 56 NA NA NA 6 145 2 114 0.75 1.56 1.55 766.10 80 76 57 NA NA NA 7 150 2 114 0.70 1.46 1.45 769.72 80 76 58 NA NA NA 8 155 2 115 0.70 1.46 1.45 773.28 80 76 56 NA NA NA 9 160 2 115 0.74 1.54 1.54 776.78 80 76 56 NA NA NA 

10 165 2 115 0.65 1.36 1.35 780.24 80 76 55 NA NA NA 11 170 2 115 0.65 1.36 1.35 783.47 81 77 54 NA NA NA 12 175 2 115 0.65 1.36 1.36 786.70 82 77 55 NA NA NA 13 180 2 115 0.60 1.26 1.25 789.99 83 77 55 NA NA NA 14 185 2 115 0.60 1.26 1.25 793.15 84 79 55 NA NA NA 15 190 2 116 0.67 1.41 1.40 796.39 85 80 55 NA NA NA 16 195 2 116 0.67 1.41 1.40 799.70 86 80 55 NA NA NA 17 200 2 116 0.71 1.49 1.49 803.00 87 81 55 NA NA NA 18 205 2 116 0.72 1.52 1.51 806.46 88 82 55 NA NA NA 19 210 2 116 0.74 1.56 1.56 809.88 88 85 55 NA NA NA 20 215 2 116 0.74 1.56 1.56 813.37 88 83 56 NA NA NA 21 220 2 116 0.71 1.50 1.50 816.89 88 83 56 NA NA NA 22 225 2 116 0.71 1.50 1.50 820.40 88 84 57 NA NA NA 23 230 2 116 0.70 1.48 1.48 823.92 87 84 57 NA NA NA 24 235 2 116 0.70 1.48 1.48 827.41 87 84 57 NA NA NA 

240 17:06 831.01

Average 240 112.9 0.66 1.36 1.36 159.385 81 78 55 #DIV/0! #DIV/0! #DIV/0! 

79.35
Company JM Mcpherson

Source Designation M-2 dust collectorTest Date 2/1/2012 Assumed Moisture (Bws) 2Test Number 3 Condensate Volume (Vlc) 15.5Operator MY Silica Gel Weight Gain (Vlc) 26.6Filter Number NA Nozzle Diameter (in.) 0.216Barometric Pressure (Pb) 30.21 Leak Rate Initial 0.00@15"Stack Static Pressure (Ps) -0.41 Leak Rate Final 0.00@6"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 4ftA Meter Corr. Factor (Y) 1.005Meter Number MB4 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.7 O2 20.67

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box Exit 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 7:33 4 96 0.76 1.49 1.45 831.65 40 39 40 NA NA NA 2 5 4 97 0.78 1.53 1.49 835.03 44 40 38 NA NA NA 3 10 4 97 0.78 1.53 1.50 838.42 46 41 38 NA NA NA 4 15 4 97 0.79 1.54 1.52 841.85 45 41 39 NA NA NA 5 20 4 97 0.78 1.53 1.50 845.29 48 41 39 NA NA NA 6 25 4 96 0.79 1.54 1.53 848.80 50 43 40 NA NA NA 7 30 4 96 0.79 1.54 1.53 852.17 50 43 40 NA NA NA 8 35 4 96 0.78 1.53 1.51 855.69 50 43 40 NA NA NA 9 40 4 96 0.73 1.43 1.42 859.02 50 44 41 NA NA NA 

10 45 4 96 0.71 1.39 1.38 862.46 51 44 41 NA NA NA 11 50 4 97 0.70 1.37 1.37 865.94 51 45 41 NA NA NA 12 55 4 97 0.69 1.35 1.35 869.39 52 45 42 NA NA NA 13 60 4 97 0.63 1.23 1.23 873.00 52 46 44 NA NA NA 14 65 4 97 0.62 1.21 1.22 876.23 52 46 42 NA NA NA 15 70 4 97 0.68 1.33 1.34 879.52 52 47 43 NA NA NA 16 75 4 96 0.68 1.33 1.34 882.79 52 47 43 NA NA NA 17 80 4 96 0.73 1.43 1.44 886.00 53 47 44 NA NA NA 18 85 4 96 0.74 1.45 1.46 889.25 53 47 44 NA NA NA 19 90 3 96 0.75 1.47 1.48 892.55 53 48 44 NA NA NA 20 95 3 96 0.76 1.49 1.51 895.84 54 48 45 NA NA NA 21 100 3 96 0.75 1.47 1.49 899.19 54 49 45 NA NA NA 22 105 3 97 0.75 1.47 1.49 902.37 55 49 45 NA NA NA 23 110 3 97 0.75 1.47 1.49 905.71 55 49 46 NA NA NA 24 115 3 97 0.75 1.47 1.49 909.05 55 50 46 NA NA NA 

120 9:33 912.41

1 120 9:41 3 97 0.60 1.17 1.20 912.41 53 51 47 NA NA NA 2 125 3 97 0.60 1.17 1.20 915.50 55 51 47 NA NA NA 3 130 3 98 0.61 1.19 1.22 918.59 56 52 47 NA NA NA 4 135 3 98 0.61 1.19 1.22 921.69 56 52 47 NA NA NA 5 140 3 99 0.60 1.17 1.21 924.79 57 52 47 NA NA NA 6 145 3 98 0.60 1.17 1.21 927.87 58 53 48 NA NA NA 7 150 3 99 0.62 1.21 1.25 931.00 58 53 48 NA NA NA 8 155 3 99 0.62 1.21 1.25 934.17 58 54 48 NA NA NA 9 160 3 99 0.64 1.25 1.29 937.16 58 54 48 NA NA NA 

10 165 3 99 0.64 1.25 1.30 940.35 58 54 49 NA NA NA 11 170 3 99 0.65 1.27 1.32 943.60 59 55 51 NA NA NA 12 175 3 99 0.65 1.27 1.32 946.92 59 55 50 NA NA NA 13 180 3 99 0.62 1.21 1.26 950.19 59 55 50 NA NA NA 14 185 3 99 0.62 1.21 1.26 953.48 58 55 50 NA NA NA 15 190 3 99 0.64 1.25 1.30 956.78 58 55 50 NA NA NA 16 195 3 99 0.64 1.26 1.31 959.97 58 55 50 NA NA NA 17 200 3 100 0.64 1.26 1.31 963.20 58 55 50 NA NA NA 18 205 3 100 0.64 1.26 1.31 966.42 58 56 50 NA NA NA 19 210 3 100 0.62 1.22 1.27 969.62 59 56 50 NA NA NA 20 215 3 100 0.62 1.22 1.27 972.76 58 55 50 NA NA NA 21 220 3 100 0.61 1.20 1.25 975.90 58 56 50 NA NA NA 22 225 3 100 0.61 1.21 1.26 979.07 58 56 50 NA NA NA 23 230 3 100 0.59 1.17 1.21 982.22 59 56 51 NA NA NA 24 235 3 100 0.59 1.17 1.22 985.45 59 56 51 NA NA NA 

240 11:41 988.70

Average 240 97.8 0.68 1.33 1.35 157.050 54.2 49.7 45.6 #DIV/0! #DIV/0! #DIV/0! 

51.94
Company JM McPherson

Source Designation 123 (M29)Test Date 1/30/2012 Assumed Moisture (Bws) 2

Test Number 1 Condensate Volume (Vlc) 34.7Operator PM PMD Silica Gel Weight Gain (Vlc) 34.6Filter Number 11121408 Nozzle Diameter (in.) 0.215Barometric Pressure (Pb) 29.99 Leak Rate Initial 0.001@12"Stack Static Pressure (Pg) -0.62 Leak Rate Final 0.002@5"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84Pitot Tube Number 5ft A Meter Corr. Factor (Y) 0.998Meter Number MB 3 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0Delta ∆H@ 1.77 O2 20.9

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Actual Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (

1 0 13:11 0 110 1.00 1.99 1.98 870.38 63 62 49 245 251 2 5 3 119 0.96 1.91 1.90 874.37 65 63 54 245 252 3 10 3 121 0.97 1.93 1.92 878.23 67 63 52 250 248 4 15 3 122 1.10 2.19 2.18 882.10 69 64 52 249 251 5 20 3 121 1.10 2.19 2.19 886.26 71 64 53 248 253 6 25 3 121 1.10 2.19 2.19 890.43 72 65 55 247 247 7 30 3 121 1.10 2.19 2.19 894.60 73 66 57 249 250 8 35 3 121 1.10 2.19 2.20 898.76 74 67 58 247 248 9 40 3 121 1.10 2.19 2.20 902.95 75 68 59 249 251 

10 45 3 121 1.10 2.19 2.20 907.12 76 68 59 248 250 11 50 3 121 0.92 1.83 1.84 911.32 77 69 59 248 250 12 55 3 122 0.92 1.83 1.84 915.17 77 69 59 249 251 13 60 3 123 0.74 1.47 1.49 919.01 77 70 58 246 249 14 65 2.5 123 0.74 1.47 1.49 922.47 77 71 57 250 251 15 70 2.5 123 0.84 1.67 1.69 925.92 77 71 55 250 249 16 75 2.5 124 0.84 1.67 1.69 929.61 78 71 56 250 249 17 80 2.5 124 0.87 1.73 1.76 933.28 78 72 55 249 250 18 85 2.5 124 0.87 1.73 1.76 937.04 79 72 55 249 250 19 90 3 124 0.90 1.79 1.82 940.77 80 73 55 241 250 20 95 3 124 0.90 1.79 1.82 944.59 80 73 54 246 248 21 100 3 124 0.92 1.83 1.87 948.42 80 74 55 248 249 22 105 3 124 0.92 1.83 1.87 952.29 81 74 54 247 250 23 110 3 124 0.82 1.63 1.67 956.15 81 74 55 246 248 24 115 2.5 124 0.82 1.63 1.67 959.78 80 75 54 250 250 

120 15:11 963.41

1 120 15:20 2 115 0.58 1.16 1.19 963.41 76 74 56 248 249 2 125 2 113 0.58 1.16 1.19 966.48 78 75 58 250 249 3 130 2.5 122 0.70 1.39 1.44 969.58 79 75 55 245 250 4 135 2.5 124 0.70 1.39 1.44 972.96 80 75 52 250 250 5 140 2.5 125 0.74 1.47 1.52 976.32 80 75 51 249 248 6 145 2.5 126 0.74 1.47 1.52 979.79 79 75 50 245 250 7 150 2.5 127 0.76 1.51 1.57 983.26 79 75 51 247 251 8 155 2.5 127 0.76 1.51 1.57 986.77 79 75 51 248 253 9 160 2.5 127 0.74 1.47 1.53 990.28 79 74 50 249 250 

10 165 2.5 127 0.74 1.47 1.53 993.75 79 74 52 247 249 11 170 2.5 127 0.70 1.39 1.45 997.19 79 74 51 249 253 12 175 2.5 126 0.70 1.39 1.45 1000.56 79 74 51 249 251 13 180 2 126 0.62 1.23 1.29 1003.91 80 74 53 249 248 14 185 2 126 0.62 1.24 1.29 1007.06 79 75 53 248 250 15 190 2.5 126 0.78 1.56 1.62 1010.22 79 75 53 250 253 16 195 2.5 126 0.78 1.56 1.62 1013.77 79 75 53 248 248 17 200 3 126 0.95 1.90 1.98 1017.31 79 75 51 245 249 18 205 3 126 0.95 1.90 1.98 1021.22 79 74 51 246 250 19 210 3 126 0.95 1.91 1.99 1025.13 79 74 51 245 249 20 215 3 126 0.95 1.91 1.99 1029.06 79 74 52 250 249 21 220 3 126 0.93 1.87 1.95 1032.98 79 74 52 250 251 22 225 3 126 0.93 1.87 1.95 1036.85 79 74 53 250 251 23 230 3 125 0.93 1.87 1.95 1040.74 79 74 53 251 248 24 235 3 125 0.93 1.88 1.95 1044.61 79 74 53 250 250 

240 17:20 1048.47

Average 240 123.4 0.86 1.72 1.76 178.090 77.1 71.8 53.9 248.0 249.9 

74.45
Company JM McPherson

Source Designation 123 (M29)Test Date 1/31/2012 Assumed Moisture (Bws) 2Test Number 2 Condensate Volume (Vlc) 40.5Operator PM PMD Silica Gel Weight Gain (Vlc) 28.2Filter Number 11121409 Nozzle Diameter (in.) 0.215Barometric Pressure (Pb) 29.85 Leak Rate Initial 0.000@10"Stack Static Pressure (Ps) -0.62 Leak Rate Final 0.001@5"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 5ft A Meter Corr. Factor (Y) 0.998Meter Number MB 3 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.77 O2 20.9

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Exp

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature DG

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (cubi

1 0 7:55 3 111 1.30 2.60 2.48 50.40 43 43 42 248 251 542 5 3 111 1.30 2.60 2.49 54.77 47 44 35 250 245 593 10 3 111 1.30 2.60 2.50 59.12 52 45 33 245 247 634 15 3 111 1.30 2.61 2.51 63.51 54 46 34 242 251 675 20 3 111 1.10 2.21 2.13 67.92 56 47 35 242 251 726 25 3 111 1.10 2.21 2.14 72.01 57 48 36 250 250 767 30 3 111 1.10 2.21 2.14 76.10 58 47 37 250 250 808 35 3 111 1.10 2.22 2.15 80.17 59 50 38 248 249 849 40 3 112 0.91 1.83 1.78 84.24 60 51 38 250 252 87

10 45 3 111 0.91 1.84 1.78 87.99 60 52 39 253 251 9111 50 2.5 112 0.84 1.70 1.65 91.75 60 52 39 248 250 9512 55 2.5 112 0.84 1.70 1.65 95.33 60 53 39 247 250 9813 60 3 112 0.97 1.96 1.92 98.91 61 54 40 250 251 10214 65 3 111 0.97 1.97 1.92 102.80 61 54 39 245 249 1015 70 3 111 0.91 1.85 1.80 106.68 62 55 38 250 250 11016 75 3 111 0.91 1.85 1.81 110.44 62 55 39 249 247 11417 80 3 110 0.89 1.81 1.77 114.20 62 55 39 250 250 11718 85 3 110 0.89 1.81 1.77 117.92 63 56 38 250 250 1219 90 3 110 0.76 1.55 1.52 121.62 64 57 40 249 249 1220 95 2.5 109 0.76 1.55 1.52 125.09 64 57 39 250 253 1221 100 2.5 105 0.68 1.39 1.36 128.52 65 58 39 251 251 1322 105 2.5 105 0.68 1.39 1.37 131.80 66 59 40 250 250 1323 110 2.5 104 0.68 1.39 1.37 135.08 67 60 41 250 251 1324 115 2.5 104 0.68 1.40 1.37 138.38 68 60 40 250 250 14

120 9:55 141.68

1 120 2.5 109 0.81 1.67 1.64 141.68 65 63 46 245 250 142 125 10:00 2.5 111 0.81 1.67 1.64 145.29 69 63 42 240 240 143 130 3 113 0.86 1.77 1.75 148.90 70 64 42 253 247 1524 135 3 113 0.86 1.77 1.75 152.61 72 64 41 249 246 155 140 3 114 0.80 1.65 1.63 156.31 73 66 43 249 250 1596 145 3 114 0.80 1.65 1.64 159.92 74 66 43 250 255 167 150 2.5 114 0.62 1.28 1.27 163.52 74 67 44 250 241 168 155 2.5 115 0.62 1.29 1.27 166.69 75 68 44 249 251 1699 160 2.5 115 0.72 1.49 1.48 169.85 75 68 45 249 249 173

10 165 2.5 115 0.72 1.50 1.48 173.28 77 69 44 249 253 1711 170 2.5 116 0.71 1.48 1.46 176.70 78 70 46 250 252 18012 175 2.5 116 0.71 1.48 1.47 180.10 79 71 46 250 252 18313 180 2.5 117 0.70 1.46 1.45 183.51 80 72 46 250 248 1814 185 2.5 117 0.70 1.46 1.45 186.90 81 73 48 249 251 19015 190 2.5 118 0.83 1.73 1.72 190.32 83 75 50 249 250 19416 195 2.5 118 0.83 1.74 1.72 194.04 84 76 49 251 250 19717 200 2.5 118 0.75 1.57 1.56 197.76 85 77 49 249 250 2018 205 2.5 118 0.75 1.57 1.56 201.31 86 78 51 249 252 20419 210 2.5 118 0.64 1.34 1.34 204.84 86 79 51 251 251 2020 215 2.5 118 0.64 1.34 1.34 208.14 88 80 51 250 249 2121 220 2.5 116 0.50 1.05 1.05 211.45 88 81 52 250 252 21422 225 2.5 115 0.50 1.05 1.05 214.38 89 82 52 251 252 21723 230 2.5 116 0.47 0.99 0.99 217.32 89 83 53 251 249 22024 235 2 115 0.47 0.99 0.99 220.14 89 83 53 250 247 222

240 12:00 222.97

Average 240 112.6 0.83 1.69 1.66 172.570 70 62 43 249 250 1

66.00
Company JM McPherson

Source Designation 123 (M29)Test Date 1/31/2012 Assumed Moisture (Bws) 2Test Number 3 Condensate Volume (Vlc) 30.2Operator PM PMD Silica Gel Weight Gain (Vlc) 38.4Filter Number 11121412 Nozzle Diameter (in.) 0.213Barometric Pressure (Pb) 29.85 Leak Rate Initial 0.001@10"Stack Static Pressure (Ps) -0.62 Leak Rate Final 0.000@5"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 5ft A Meter Corr. Factor (Y) 0.998Meter Number MB 3 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0

Delta ∆H@ 1.77 O2 20.9

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Exp

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature DG

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (cubi

1 0 13:05 3.5 120 1.30 2.55 2.51 223.28 76 76 62 245 250 2272 5 3.5 120 1.30 2.55 2.51 227.78 77 76 60 248 250 2323 10 3.5 120 1.30 2.55 2.52 232.30 80 76 48 251 245 234 15 3.5 120 1.30 2.55 2.52 236.82 81 76 47 248 250 245 20 3.5 121 1.20 2.35 2.33 241.35 83 76 49 249 252 246 25 3.5 121 1.20 2.35 2.33 245.72 84 77 48 250 249 2507 30 3 121 0.99 1.94 1.93 250.09 84 77 49 250 250 2548 35 3 121 0.99 1.94 1.93 254.08 85 78 49 249 252 259 40 3 122 0.92 1.80 1.80 258.06 85 78 50 251 253 26

10 45 3 123 0.92 1.80 1.80 261.91 85 78 50 249 246 2611 50 3 124 0.87 1.71 1.71 265.73 86 79 50 251 248 26912 55 3 124 0.87 1.71 1.71 269.45 87 79 50 251 251 2713 60 3 124 0.94 1.84 1.85 273.16 87 80 51 249 245 27714 65 3 124 0.94 1.84 1.85 277.04 88 81 51 250 251 28015 70 3.5 124 1.10 2.16 2.17 280.94 89 81 52 248 250 2816 75 3.5 124 1.10 2.16 2.17 285.15 90 82 50 249 244 28917 80 3.5 125 1.10 2.16 2.18 289.38 90 83 51 249 247 29318 85 3.5 124 1.10 2.16 2.18 293.61 91 83 50 249 245 29719 90 3.5 124 1.10 2.16 2.18 297.85 91 84 51 251 245 30220 95 3.5 125 1.10 2.16 2.18 302.08 92 84 51 252 250 3021 100 3.5 125 0.98 1.92 1.95 306.32 92 85 52 249 251 31022 105 3.5 125 0.98 1.92 1.95 310.32 92 85 53 251 250 31423 110 3.5 125 0.98 1.92 1.95 314.33 93 86 54 250 248 3124 115 3.5 126 0.98 1.92 1.96 318.33 94 87 55 252 253 322

120 15:05 322.34

1 120 15:10 3.5 126 1.30 2.55 2.61 322.34 90 88 55 243 245 322 125 4 126 1.30 2.55 2.61 326.95 93 88 55 240 246 333 130 4 127 1.20 2.35 2.42 331.57 95 88 52 235 248 334 135 4 128 1.20 2.35 2.42 336.02 95 88 52 242 250 3405 140 4 128 1.10 2.16 2.22 340.47 95 88 54 248 249 3446 145 4 128 1.10 2.16 2.22 344.74 96 88 53 245 248 347 150 4 128 1.10 2.16 2.23 348.99 97 89 55 240 250 358 155 3.5 128 1.10 2.16 2.23 353.25 97 89 56 240 252 3579 160 3.5 129 0.93 1.82 1.89 357.50 97 90 57 245 251 36

10 165 3.5 129 0.93 1.82 1.89 361.42 98 90 56 240 249 3611 170 3.5 129 0.83 1.63 1.69 365.36 98 91 56 239 248 36912 175 3 129 0.83 1.63 1.69 369.07 98 91 56 235 248 37213 180 3 129 0.85 1.67 1.73 372.78 98 91 57 238 249 3714 185 3 129 0.85 1.67 1.74 376.54 97 92 56 256 253 38015 190 3 129 0.80 1.57 1.64 380.30 97 92 56 250 251 3816 195 3 130 0.80 1.57 1.64 383.94 97 92 57 255 247 38717 200 3 130 0.75 1.48 1.54 387.56 97 92 58 251 252 3918 205 3 130 0.75 1.48 1.54 391.07 97 92 58 250 249 39419 210 3 130 0.70 1.38 1.44 394.59 98 92 57 251 251 39720 215 3 129 0.70 1.38 1.44 397.99 98 92 58 250 250 4021 220 3 129 0.64 1.27 1.32 401.42 98 93 58 250 250 40422 225 3 129 0.64 1.27 1.32 404.70 98 93 58 250 251 40723 230 3 127 0.64 1.27 1.32 407.95 98 93 58 249 250 4124 235 3 124 0.64 1.27 1.32 411.23 97 93 58 249 249 414

240 17:10 414.50

Average 240 125.7 0.98 1.93 1.96 191.220 91.7 85.5 53.7 247.5 249.2 32

88.57
Company JM McPherson

Source Designation 123 DCTest Date 1/30/2012 Assumed Moisture (Bws) 2

Test Number 1 Condensate Volume (Vlc) 36.2Operator JP Silica Gel Weight Gain (Vlc) 36.9Filter Number Nozzle Diameter (in.) 0.216Barometric Pressure (Pb) 29.99 Leak Rate Initial 0.005 @14"Stack Static Pressure (Pg) -0.62 Leak Rate Final 0.017 @ 7"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84Pitot Tube Number 4 ft A Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0.25Delta ∆H@ 1.72 O2 20.51

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Actual Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box E

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperatu

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 13:00 6 122 1.30 2.55 2.48 535.07 56 56 51 NA NA NA 2 5 6 121 1.30 2.55 2.48 539.52 58 56 52 NA NA NA 3 10 6 120 1.25 2.45 2.39 543.93 61 57 50 NA NA NA 4 15 6 120 1.25 2.45 2.40 548.28 64 57 51 NA NA NA 5 20 5.5 119 1.15 2.26 2.22 552.64 66 58 52 NA NA NA 6 25 5.5 119 1.15 2.26 2.22 556.87 68 59 53 NA NA NA 7 30 5 119 1.05 2.06 2.04 561.09 69 59 54 NA NA NA 8 35 5 118 1.05 2.06 2.04 565.17 71 60 55 NA NA NA 9 40 4.5 119 0.94 1.85 1.83 569.22 71 61 56 NA NA NA 

10 45 4.5 119 0.95 1.86 1.86 573.07 72 62 57 NA NA NA 11 50 4 119 0.76 1.49 1.49 576.93 73 62 57 NA NA NA 12 55 4 120 0.76 1.49 1.49 580.51 73 63 56 NA NA NA 13 60 4.5 120 0.95 1.86 1.87 583.94 72 63 53 NA NA NA 14 65 4.5 121 0.95 1.86 1.87 587.82 73 64 50 NA NA NA 15 70 4.5 121 0.92 1.81 1.82 591.71 73 64 49 NA NA NA 16 75 4.5 121 0.92 1.81 1.82 595.54 73 65 48 NA NA NA 17 80 4 121 0.84 1.65 1.66 599.35 74 65 49 NA NA NA 18 85 4 121 0.85 1.67 1.69 603.01 74 65 49 NA NA NA 19 90 4 121 0.76 1.49 1.51 606.70 75 66 49 NA NA NA 20 95 4 120 0.76 1.49 1.51 610.22 75 66 49 NA NA NA 21 100 3.5 117 0.73 1.43 1.46 613.73 75 66 50 NA NA NA 22 105 3.5 116 0.72 1.41 1.44 617.15 75 67 49 NA NA NA 23 110 3.5 116 0.63 1.24 1.26 620.54 76 67 49 NA NA NA 24 115 3.5 116 0.61 1.20 1.22 623.75 76 68 49 NA NA NA 

120 15:11 626.96

1 120 15:20 4.5 122 0.90 1.77 1.81 626.96 69 68 51 NA NA NA 2 125 4.5 122 0.90 1.77 1.81 630.75 75 68 48 NA NA NA 3 130 4.5 122 0.92 1.81 1.85 634.57 76 69 47 NA NA NA 4 135 4.5 123 0.92 1.81 1.86 638.42 77 69 45 NA NA NA 5 140 4.5 123 0.89 1.75 1.80 642.27 78 69 46 NA NA NA 6 145 4.5 124 0.87 1.71 1.76 646.08 78 69 47 NA NA NA 7 150 4 124 0.83 1.63 1.68 649.83 78 70 49 NA NA NA 8 155 4 124 0.83 1.63 1.68 653.45 78 70 48 NA NA NA 9 160 4 124 0.74 1.45 1.50 657.06 78 70 48 NA NA NA 

10 165 4 124 0.73 1.43 1.49 660.53 78 70 48 NA NA NA 11 170 3.5 123 0.63 1.24 1.28 663.97 78 70 47 NA NA NA 12 175 3.5 123 0.63 1.24 1.29 667.16 78 70 48 NA NA NA 13 180 3.5 123 0.70 1.37 1.43 670.32 78 70 48 NA NA NA 14 185 3.5 123 0.70 1.38 1.43 673.71 78 70 48 NA NA NA 15 190 4 123 0.73 1.44 1.49 677.09 79 70 47 NA NA NA 16 195 4 123 0.73 1.44 1.50 680.53 79 71 47 NA NA NA 17 200 4 123 0.78 1.54 1.60 683.95 78 71 47 NA NA NA 18 205 4 123 0.77 1.52 1.58 687.51 78 71 47 NA NA NA 19 210 3.5 123 0.70 1.38 1.44 691.02 78 71 47 NA NA NA 20 215 3.5 123 0.70 1.39 1.44 694.41 77 70 47 NA NA NA 21 220 3.5 120 0.65 1.29 1.34 697.74 77 7\0 47 NA NA NA 22 225 3.5 121 0.65 1.29 1.34 701.00 77 70 47 NA NA NA 23 230 3.5 121 0.62 1.23 1.28 704.21 77 70 46 NA NA NA 24 235 3.5 122 0.62 1.23 1.28 707.38 77 70 47 NA NA NA 

240 17:20 710.56

Average 240 121.1 0.85 1.67 1.69 175.487 73.9 66.0 49.5 #DIV/0! #DIV/0! #DIV/0! 

69.95
Company JM McPherson

Source Designation Lines 123 DCTest Date 1/31/2012 Assumed Moisture (Bws) 2Test Number 2 Condensate Volume (Vlc) 40.4Operator JP Silica Gel Weight Gain (Vlc) 32.9Filter Number NA Nozzle Diameter (in.) 0.216Barometric Pressure (Pb) 29.85 Leak Rate Initial .005 @ 12"Stack Static Pressure (Ps) -0.62 Leak Rate Final .004 @7"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 4 ft A Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0.25

Delta ∆H@ 1.72 O2 20.51

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box Exit 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 7:55 4.5 110 0.90 1.77 1.70 710.80 40 40 37 NA NA NA 2 5 4.5 109 0.90 1.78 1.70 714.40 40 40 35 NA NA NA 3 10 5 110 1.00 1.97 1.89 718.00 43 41 35 NA NA NA 4 15 5 110 1.00 1.98 1.90 721.79 46 41 34 NA NA NA 5 20 5 110 1.00 1.98 1.90 725.60 49 41 34 NA NA NA 6 25 5 110 1.00 1.98 1.91 729.48 51 42 35 NA NA NA 7 30 5 110 1.05 2.08 2.01 733.30 53 43 35 NA NA NA 8 35 5 110 1.05 2.09 2.01 737.24 55 44 35 NA NA NA 9 40 4.5 110 0.89 1.77 1.71 741.18 56 45 35 NA NA NA 

10 45 4.5 110 0.89 1.77 1.72 744.88 57 45 35 NA NA NA 11 50 4.5 110 0.80 1.59 1.55 748.52 57 46 34 NA NA NA 12 55 4.5 110 0.80 1.60 1.55 752.02 58 47 34 NA NA NA 13 60 4.5 110 0.86 1.72 1.67 755.51 59 47 35 NA NA NA 14 65 4.5 109 0.86 1.72 1.67 759.11 60 48 35 NA NA NA 15 70 4.5 109 0.90 1.80 1.75 762.76 60 49 35 NA NA NA 16 75 4.5 109 0.90 1.80 1.76 766.49 61 50 35 NA NA NA 17 80 5 109 0.95 1.91 1.86 770.20 62 50 35 NA NA NA 18 85 5 109 0.95 1.91 1.86 774.03 63 51 36 NA NA NA 19 90 5 108 0.95 1.91 1.87 777.89 64 52 35 NA NA NA 20 95 5 108 0.95 1.91 1.87 781.73 65 53 36 NA NA NA 21 100 4.5 108 0.88 1.77 1.74 785.57 66 54 36 NA NA NA 22 105 4.5 108 0.88 1.78 1.74 789.29 67 55 36 NA NA NA 23 110 4.5 108 0.91 1.84 1.80 793.03 68 56 37 NA NA NA 24 115 4.5 108 0.90 1.82 1.79 796.81 70 57 37 NA NA NA 

120 9:55 800.61

1 120 10:00 3.5 107 0.61 1.24 1.22 800.61 62 59 38 NA NA NA 2 125 3.5 107 0.60 1.22 1.20 803.70 68 59 38 NA NA NA 3 130 3.5 108 0.64 1.30 1.28 806.79 69 60 39 NA NA NA 4 135 3.5 108 0.64 1.30 1.29 809.97 71 61 39 NA NA NA 5 140 3.5 108 0.67 1.37 1.35 813.17 71 61 39 NA NA NA 6 145 3.5 110 0.68 1.39 1.37 816.47 73 62 39 NA NA NA 7 150 4 111 0.71 1.45 1.43 819.78 73 63 39 NA NA NA 8 155 4 112 0.71 1.45 1.44 823.16 74 63 40 NA NA NA 9 160 4 112 0.67 1.37 1.36 826.54 74 64 40 NA NA NA 

10 165 4 113 0.67 1.37 1.36 829.85 75 65 40 NA NA NA 11 170 3.5 113 0.66 1.35 1.34 833.13 76 65 40 NA NA NA 12 175 3.5 113 0.66 1.36 1.34 836.41 77 66 41 NA NA NA 13 180 4 114 0.78 1.60 1.59 839.68 78 67 42 NA NA NA 14 185 4 114 0.78 1.61 1.59 843.21 80 68 43 NA NA NA 15 190 4.5 114 0.88 1.81 1.80 846.78 81 69 43 NA NA NA 16 195 4.5 114 0.88 1.82 1.80 850.55 82 70 45 NA NA NA 17 200 5 114 0.94 1.94 1.93 854.38 84 71 45 NA NA NA 18 205 5 115 0.94 1.94 1.93 858.30 84 72 46 NA NA NA 19 210 5 115 0.97 2.01 2.00 862.24 85 73 47 NA NA NA 20 215 5 115 0.97 2.01 2.01 866.28 87 75 47 NA NA NA 21 220 5 116 0.95 1.97 1.97 870.30 87 75 47 NA NA NA 22 225 5 116 0.95 1.97 1.97 874.30 88 77 47 NA NA NA 23 230 5 117 0.93 1.93 1.93 878.34 88 78 48 NA NA NA 24 235 5 116 0.93 1.94 1.93 882.27 89 78 47 NA NA NA 

240 12:00 886.25

Average 240 110.9 0.85 1.73 1.70 175.447 68 57 39 #DIV/0! #DIV/0! #DIV/0! 

62.54
Company JM McPherson

Source Designation Line 123 DCTest Date 1/31/2012 Assumed Moisture (Bws) 2Test Number 3 Condensate Volume (Vlc) 31.54Operator JP Silica Gel Weight Gain (Vlc) 41Filter Number NA Nozzle Diameter (in.) 0.216Barometric Pressure (Pb) 29.85 Leak Rate Initial .000 @ 15"Stack Static Pressure (Ps) -0.62 Leak Rate Final .011 @7"Stack Dimensions 1 (in.) 38 Traverse points 24*Stack Dimensions 2 (in.) Pitot Corr. Factor (Cp) 0.84

Pitot Tube Number 4 ft A Meter Corr. Factor (Y) 1.006Meter Number 6 Fyrite Results (%)Meter Isokinetic Factor (Kiso) CO2 0.25

Delta ∆H@ 1.72 O2 20.51

Traverse Sampling Time Sampling Stack Temp.Velocity Pres. Desired Orifice Orifice Sample Volume Dry Gas Meter Temp. Last Impinger Probe Filter Box Filter Box Exit 

Point (Minutes) Clock Time Train Vac. (F) ("H2O) Differential Differential (cubic feet) Inlet Outlet Temperature Temperature Temperature Temperature 

Number ø (24 hour) ("Hg) Ts ∆Ps ("H2O) ∆H ("H2O) ∆H Vm (F) Tm (F) Tm (F) (F) (F) (F) 

1 0 13:05 3.5 117 0.75 1.49 1.47 886.52 67 67 57 NA NA NA 2 5 3.5 117 0.75 1.49 1.47 889.99 67 66 43 NA NA NA 3 10 3.5 116 0.79 1.57 1.55 893.43 66 66 42 NA NA NA 4 15 3.5 117 0.79 1.57 1.56 896.95 69 66 41 NA NA NA 5 20 3.5 117 0.84 1.67 1.66 900.49 72 66 41 NA NA NA 6 25 3.5 118 0.83 1.65 1.64 904.17 74 66 41 NA NA NA 7 30 3.5 118 0.85 1.69 1.68 907.79 76 67 42 NA NA NA 8 35 3.5 119 0.86 1.71 1.71 911.46 78 68 42 NA NA NA 9 40 4 120 0.92 1.83 1.83 915.20 79 69 41 NA NA NA 

10 45 4 120 0.92 1.83 1.83 919.06 80 70 42 NA NA NA 11 50 4 121 0.97 1.93 1.93 922.91 81 70 42 NA NA NA 12 55 4 121 0.97 1.93 1.94 926.87 82 71 42 NA NA NA 13 60 3.5 121 0.83 1.65 1.66 930.83 83 72 43 NA NA NA 14 65 3.5 121 0.83 1.65 1.66 934.52 83 73 43 NA NA NA 15 70 4 121 0.94 1.87 1.89 938.20 83 73 43 NA NA NA 16 75 4 121 0.94 1.87 1.89 942.13 84 74 43 NA NA NA 17 80 4.5 121 1.05 2.09 2.12 946.05 84 74 43 NA NA NA 18 85 4.5 121 1.05 2.09 2.12 950.21 84 75 44 NA NA NA 19 90 4.5 122 1.10 2.19 2.22 954.38 85 75 45 NA NA NA 20 95 4.5 122 1.10 2.19 2.23 958.62 85 75 46 NA NA NA 21 100 5 122 1.20 2.39 2.43 962.87 86 76 46 NA NA NA 22 105 5 122 1.20 2.39 2.44 967.30 87 76 46 NA NA NA 23 110 5 122 1.25 2.49 2.54 971.78 88 77 47 NA NA NA 24 115 5 122 1.25 2.49 2.55 976.35 88 78 47 NA NA NA 

120 15:05 980.93

1 120 15:10 4 122 0.89 1.77 1.82 980.93 80 78 49 NA NA NA 2 125 4 123 0.89 1.77 1.82 984.74 84 78 45 NA NA NA 3 130 4.5 124 0.92 1.83 1.88 988.55 84 78 45 NA NA NA 4 135 4.5 124 0.92 1.83 1.89 992.48 85 78 44 NA NA NA 5 140 4.5 125 0.99 1.97 2.03 996.41 86 78 45 NA NA NA 6 145 4.5 125 0.99 1.97 2.04 1000.44 87 78 45 NA NA NA 7 150 4.5 125 1.00 1.99 2.06 1004.50 87 78 47 NA NA NA 8 155 4.5 125 1.00 1.99 2.06 1008.60 87 79 47 NA NA NA 9 160 4.5 125 0.96 1.91 1.98 1012.70 87 79 47 NA NA NA 

10 165 4.5 125 0.96 1.91 1.98 1016.72 88 79 48 NA NA NA 11 170 4 125 0.83 1.65 1.72 1020.76 88 79 48 NA NA NA 12 175 4 125 0.83 1.65 1.72 1024.49 87 79 48 NA NA NA 13 180 4 125 0.80 1.59 1.66 1028.21 87 79 48 NA NA NA 14 185 4 125 0.80 1.60 1.66 1031.89 87 79 48 NA NA NA 15 190 4 125 0.84 1.68 1.75 1035.55 87 79 48 NA NA NA 16 195 4 125 0.84 1.68 1.75 1039.33 87 79 48 NA NA NA 17 200 4 125 0.86 1.72 1.79 1043.06 88 80 48 NA NA NA 18 205 4 126 0.86 1.72 1.80 1046.82 88 80 48 NA NA NA 19 210 4 126 0.88 1.77 1.84 1050.64 90 81 49 NA NA NA 20 215 4 126 0.88 1.77 1.84 1054.45 90 81 50 NA NA NA 21 220 4 126 0.88 1.77 1.84 1058.29 91 81 51 NA NA NA 22 225 4 126 0.88 1.77 1.85 1062.15 91 82 51 NA NA NA 23 230 4 126 0.86 1.73 1.81 1066.01 91 82 51 NA NA NA 24 235 4 126 0.86 1.74 1.81 1069.83 91 83 52 NA NA NA 

240 17:10 1073.67

Average 240 122.5 0.93 1.85 1.88 187.150 83.5 75.4 45.9 #DIV/0! #DIV/0! #DIV/0! 

79.44

























































Appendix B 

 Process Data 
Appendix C 

Equipment Calibration Documents 






METHOD 5 DRY GAS METER CALIBRATION USING CRITICAL ORIFICES

1) Select three critical orifices to calibrate the dry gas meter which bracket the expected operating range.2) Record barometric pressure before and after calibration procedure.3) Run at tested vacuum (from Orifice Calibration Report), for a period of time

necessary to achieve a minimum total volume of 5 cubic feet.

4) Record data and information in the GREEN cells, YELLOW cells are calculated.

INITIAL FINAL AVG (Pbar)

DATE: 1/5/2012 METER SERIAL #: 1817 BAROMETRIC PRESSURE (in Hg): 29.95 29.91 29.93 

METER PART #: MB 6 CRITICAL ORIFICE SET SERIAL #: 1447 

K' TESTED TEMPERATURES °F ELAPSED

FACTOR VACUUM DGM READINGS (FT3

) AMBIENT DGM INLET DGM OUTLET DGM TIME (MIN) DGM ΔH (1) 

ORIFICE # RUN # (AVG) (in Hg) INITIAL FINAL NET (Vm) INITIAL FINAL INITIAL FINAL AVG θ (in H2O) Vm (STD) V

1 0.8778 16 430.30 437.034 6.734 56 57 58 57 57 57.25 6.00 4.1 6.9469 2 0.8778 16 437.034 443.782 6.748 56 58 60 57 57 58 6.00 4.1 6.9513 3 0.8778 16 443.782 450.527 6.745 56 60 62 57 57 59 6.00 4.1 6.9348 1 0.5057 16 450.527 456.293 5.766 56 62 62 57 58 59.75 9.00 1.3 5.8794 2 0.5057 16 456.293 462.078 5.785 56 62 63 58 58 60.25 9.00 1.3 5.8931 3 0.5057 16 462.078 467.874 5.796 56 63 64 58 59 61 9.00 1.3 5.8958 1 0.3367 16 467.874 473.129 5.255 55 64 62 59 59 61 12.00 0.59 5.3361 2 0.3367 16 473.129 478.382 5.253 55 62 63 59 59 60.75 12.00 0.59 5.3367 3 0.3367 16 478.382 483.632 5.250 55 63 62 59 59 60.75 12.00 0.59 5.3336 

(1) = Net volume of gas sample passed through DGM, corrected to standard conditions

K1 = 17.64 oR/in. Hg (English), 0.3858 oK/mm Hg (Metric) AVERAGE DRY GAS METER CALIBRATION FAC

Tm = Absolute DGM avg. temperature (oR - English, oK - Metric)

ΔH@ = 0.75 θ ΔH Vm(std) AVERA

(2) = Volume of gas sample passed through the critical orifice, corrected to standard con

Vcr(std) Vm

Tamb = Absolute ambient temperature (oR - English, oK - Metric)

K' = Average K' factor from Critical Orifice Calibration

(3) = DGM calibration factor

321812
METHOD 5 DRY GAS METER CALIBRATION USING CRITICAL ORIFICES

1) Select three critical orifices to calibrate the dry gas meter which bracket the expected operating range.2) Record barometric pressure before and after calibration procedure.3) Run at tested vacuum (from Orifice Calibration Report), for a period of time

necessary to achieve a minimum total volume of 5 cubic feet.

4) Record data and information in the GREEN cells, YELLOW cells are calculated.

INITIAL FINAL AVG (Pbar)

DATE: 1/20/2012 METER SERIAL #: 1672 BAROMETRIC PRESSURE (in Hg): 30.27 30.29 30.28 

METER PART #: MB5 CRITICAL ORIFICE SET SERIAL #: 1447 

K' TESTED TEMPERATURES °F ELAPSED

FACTOR VACUUM DGM READINGS (FT3

) AMBIENT DGM INLET DGM OUTLET DGM TIME (MIN) DGM ΔH (1) 

ORIFICE # RUN # (AVG) (in Hg) INITIAL FINAL NET (Vm) INITIAL FINAL INITIAL FINAL AVG θ (in H2O) Vm (STD) Vcr 

1 0.8778 15 679.220 685.945 6.725 55 55 55 55 55 55 6.00 3.7 7.0418 7.2 0.8778 15 685.945 692.708 6.763 55 55 56 55 55 55.25 6.00 3.7 7.0782 7.3 0.8778 15 692.708 699.442 6.734 55 56 59 55 56 56.5 6.00 3.7 7.0308 7.1 0.5057 16 699.442 705.210 5.768 55 59 61 56 56 58 9.00 1.2 5.9686 6.2 0.5057 16 705.210 710.990 5.780 60 61 62 56 57 59 9.00 1.2 5.9695 6.3 0.5057 16 710.990 716.767 5.777 61 62 64 57 58 60.25 9.00 1.2 5.9521 6.1 0.3367 16 716.767 722.024 5.257 62 64 65 58 60 61.75 12.00 0.53 5.3920 5.2 0.3367 16 722.024 727.285 5.261 62 65 66 60 61 63 12.00 0.53 5.3832 5.3 0.3367 16 727.285 732.552 5.267 63 66 67 61 63 64.25 12.00 0.53 5.3764 5.

AVERAGE DRY GAS METER CALIBRATION FACT

AVERAG

(1) = Net volume of gas sample passed through DGM, corrected to standard conditions

K1 = 17.64 oR/in. Hg (English), 0.3858 oK/mm Hg (Metric)

Tm = Absolute DGM avg. temperature (oR - English, oK - Metric) ΔH@ = 0.

Vcr

(2) = Volume of gas sample passed through the critical orifice, corrected to standard conditions

Tamb = Absolute ambient temperature (oR - English, oK - Metric)

K' = Average K' factor from Critical Orifice Calibration

(3) = DGM calibration factor

321812

ENVIRONMENTAL 

USING THE CRITICAL ORIFICES AS CALIBRATION STANDARDS:The following equations are used to calculate the standard volumes of air passed through the DGM, Vm (std), and the critical 

orifice, Vcr (std), and the DGM calibration factor, Y. These equations are automatically calculated in the spreadsheet above.

(

Tm

Pbar

H Vm std

K Vm /( 13 )6. 1)( Δ+ ∗∗=

Tamb

Pbar Vcr std

K Θ∗ )( '∗=

)(

)(

std

std

Vm

Vcr

Y =
METHOD 5 DRY GAS METER CALIBRATION USING CRITICAL ORIFICE

S

1) Select three critical orifices to calibrate the dry gas meter which bracket the expected operating range.2) Record barometric pressure before and after calibration procedure.3) Run at tested vacuum (from Orifice Calibration Report), for a period of time

necessary to achieve a minimum total volume of 5 cubic feet.

4) Record data and information in the GREEN cells, YELLOW cells are calculated.

INITIAL FINAL AVG (Pbar)

DATE: 12/16/2011 METER SERIAL #: CA 4 BAROMETRIC PRESSURE (in Hg): 30.29 30.26 30.275 

METER PART #: MB4 CRITICAL ORIFICE SET SERIAL #: 1447 

K' TESTED TEMPERATURES °F ELAPSED

FACTOR VACUUM DGM READINGS (FT3

) AMBIENT DGM INLET DGM OUTLET DGM TIME (MIN) DGM ΔH (1) 

ORIFICE # RUN # (AVG) (in Hg) INITIAL FINAL NET (Vm) INITIAL FINAL INITIAL FINAL AVG θ (in H2O) Vm (STD) Vc

1 0.6665 15 466.570 471.750 5.180 63 63 63 63 62 62.75 6.00 2.3 5.3247 52 0.6665 15 471.750 476.960 5.210 62 63 63 62 62 62.5 6.00 2.3 5.3581 53 0.6665 15 476.960 482.160 5.20 61 63 64 62 63 63 6.00 2.3 5.3427 51 0.5057 15 482.50 488.260 5.760 65 65 65 63 63 64 9.00 1.3 5.8925 62 0.5057 15 488.260 494.030 5.770 62 65 66 63 63 64.25 9.00 1.3 5.8999 63 0.5057 15 494.030 499.80 5.770 63 66 67 63 64 65 9.00 1.3 5.8915 61 0.3367 15 500.0 505.250 5.250 64 66 66 64 64 65 12.00 0.6 5.3515 52 0.3367 15 505.250 510.510 5.260 62 66 67 64 65 65.5 12.00 0.6 5.3565 53 0.3367 15 510.510 516.650 6.140 63 67 68 65 65 66.25 14.00 0.6 6.2438 6

AVERAGE DRY GAS METER CALIBRATION FAC

AVERAG

(1) = Net volume of gas sample passed through DGM, corrected to standard conditions

K1 = 17.64 oR/in. Hg (English), 0.3858 oK/mm Hg (Metric)

Tm = Absolute DGM avg. temperature (oR - English, oK - Metric) ΔH@ = 0

Vc

(2) = Volume of gas sample passed through the critical orifice, corrected to standard conditions

Tamb = Absolute ambient temperature (oR - English, oK - Metric)

K' = Average K' factor from Critical Orifice Calibration

(3) = DGM calibration factor

241812

ENVIRONMENTAL 

USING THE CRITICAL ORIFICES AS CALIBRATION STANDARDS:The following equations are used to calculate the standard volumes of air passed through the DGM, Vm (std), and the critical 

orifice, Vcr (std), and the DGM calibration factor, Y. These equations are automatically calculated in the spreadsheet above.

(

Tm

Pbar

H Vm std

K Vm /( 13 )6. 1)( Δ+ ∗∗=

Tamb

Pbar Vcr std

K Θ∗ )( '∗=

)(

)(

std

std

Vm

Vcr

Y =
METHOD 5 DRY GAS METER CALIBRATION USING CRITICAL ORIFICES

1) Select three critical orifices to calibrate the dry gas meter which bracket the expected operating range.2) Record barometric pressure before and after calibration procedure.3) Run at tested vacuum (from Orifice Calibration Report), for a period of time

necessary to achieve a minimum total volume of 5 cubic feet.

4) Record data and information in the GREEN cells, YELLOW cells are calculated.

INITIAL FINAL AVG (Pbar)

DATE: 1/13/2012 METER SERIAL #: C-5000 BAROMETRIC PRESSURE (in Hg): 29.54 29.54 29.54 

METER PART #: MB3 CRITICAL ORIFICE SET SERIAL #: 1447 

K' TESTED TEMPERATURES °F ELAPSED

FACTOR VACUUM DGM READINGS (FT3

) AMBIENT DGM INLET DGM OUTLET DGM TIME (MIN) DGM ΔH (1) 

ORIFICE # RUN # (AVG) (in Hg) INITIAL FINAL NET (Vm) INITIAL FINAL INITIAL FINAL AVG θ (in H2O) Vm (STD) Vcr 

1 0.8778 16 602.70 609.330 6.630 67 52 54 50 52 52 6.00 4.1 6.8206 6.2 0.8778 16 609.330 615.980 6.650 66 54 57 52 53 54 6.00 4.1 6.8146 6.3 0.8778 16 615.980 622.670 6.690 66 57 61 53 55 56.5 6.00 4.1 6.8224 6.1 0.5057 16 623.0 628.760 5.760 65 60 63 56 58 59.25 9.00 1.3 5.8025 5.2 0.5057 16 628.760 634.550 5.790 66 63 66 58 60 61.75 9.00 1.3 5.8048 5.3 0.5057 16 634.550 640.340 5.790 67 66 68 60 62 64 9.00 1.3 5.7798 5.1 0.3367 16 640.50 645.810 5.310 66 66 68 62 64 65 12.00 0.58 5.2811 5.2 0.3367 16 645.810 651.120 5.310 67 68 70 64 65 66.75 12.00 0.58 5.2636 5.3 0.3367 16 651.120 656.460 5.340 67 70 70 65 67 68 12.00 0.58 5.2808 5.

AVERAGE DRY GAS METER CALIBRATION FACT

AVERAG

(1) = Net volume of gas sample passed through DGM, corrected to standard conditions

K1 = 17.64 oR/in. Hg (English), 0.3858 oK/mm Hg (Metric)

Tm = Absolute DGM avg. temperature (oR - English, oK - Metric) ΔH@ = 0.

Vcr

(2) = Volume of gas sample passed through the critical orifice, corrected to standard conditions

Tamb = Absolute ambient temperature (oR - English, oK - Metric)

K' = Average K' factor from Critical Orifice Calibration

(3) = DGM calibration factor

321812

ENVIRONMENTAL 

USING THE CRITICAL ORIFICES AS CALIBRATION STANDARDS:The following equations are used to calculate the standard volumes of air passed through the DGM, Vm (std), and the critical 

orifice, Vcr (std), and the DGM calibration factor, Y. These equations are automatically calculated in the spreadsheet above.

(

Tm

Pbar

H Vm std

K Vm /( 13 )6. 1)( Δ+ ∗∗=

Tamb

Pbar Vcr std

K Θ∗ )( '∗=

)(

)(

std

std

Vm

Vcr

Y =








Line 123, O2 and CO2 Concentrations

Johns Manville

McPherson, Kansas

BTEC Project No. 11-4191.03

Sampling Dates: January 30 and 31, 2012

Parameter Run 1 Run 2 Run 3 Average O2 Correction

Test Run Date 1/30/2012 1/31/2012 1/31/2012 Co 0.03 -0.01 -0.03

Cma 9.95 9.95 9.95

Oxygen Concentration (%) 20.65 20.73 20.71 20.70 Cm 10.05 10.04 10.03Oxygen Concentration (%, drift corrected as per USEPA 7E) 20.48 20.54 20.51 20.51Carbon Dioxide Concentration (%) 0.28 0.26 0.22 0.25 CO2 Correction

Carbon Dioxide Concentration (%, drift corrected as per USEPA 7E) 0.28 0.26 0.22 0.25

Co 0.00 0.00 0.00Cma 10.1 10.1 10.1Cm 10.10 10.11 10.11

Co= Average of initial and final zero gasesCma=Actual concentration of the calibration gas

Cm= Average of initial and final calibration gases

Revision 1.0 - 1/5/2012 - BC
Line 122, Module 1 O2 and CO2 Concentrations

Johns Manville

McPherson, Kansas

BTEC Project No. 11-4191.03

Sampling Dates: February 1 and 2, 2012

Parameter Run 1 Run 2 Run 3 Average O2 Correction

Test Run Date 2/1/2012 2/1/2012 2/2/2012 Co -0.01 -0.01 -0.05

Cma 9.95 9.95 9.95

Oxygen Concentration (%) 20.75 20.86 20.84 20.82 Cm 10.02 10.01 10.01Oxygen Concentration (%, drift corrected as per USEPA 7E) 20.60 20.72 20.68 20.67Carbon Dioxide Concentration (%) 0.00 0.00 0.00 0.00 CO2 Correction

Carbon Dioxide Concentration (%, drift corrected as per USEPA 7E) 0.00 0.00 -0.01 0.00

Co 0.00 0.00 0.01Cma 10.1 10.1 10.1Cm 10.12 10.07 10.13

Co= Average of initial and final zero gasesCma=Actual concentration of the calibration gas

Cm= Average of initial and final calibration gases

Revision 1.0 - 1/5/2012 - BC
Line 122, Module 2 O2 and CO2 Concentrations

Johns Manville

McPherson, Kansas

BTEC Project No. 11-4191.03

Sampling Dates: February 1 and 2, 2012

Parameter Run 1 Run 2 Run 3 Average O2 Correction

Test Run Date 2/1/2012 2/1/2012 2/2/2012 Co -0.01 -0.01 -0.05

Cma 9.95 9.95 9.95

Oxygen Concentration (%) 20.74 20.86 20.84 20.81 Cm 10.02 10.01 10.01Oxygen Concentration (%, drift corrected as per USEPA 7E) 20.59 20.72 20.68 20.67Carbon Dioxide Concentration (%) 0.00 0.00 0.00 0.00 CO2 Correction

Carbon Dioxide Concentration (%, drift corrected as per USEPA 7E) 0.00 0.00 -0.01 0.00

Co 0.00 0.00 0.01Cma 10.1 10.1 10.1Cm 10.12 10.07 10.13

Co= Average of initial and final zero gasesCma=Actual concentration of the calibration gas

Cm= Average of initial and final calibration gases

Revision 1.0 - 1/5/2012 - BC
Appendix D 

Laboratory Analytical Results 
Your Project #: 11-4191.05 

Site Location: JM MCPHERSON 

Attention: James K. Sharp

BT Environmental Consulting

4949 Fernlee Avenue

Royal Oak, MI

USA 48073

Report Date: 2012/02/16

CERTIFICATE OF ANALYSIS

MAXXAM JOB #: B218757

Received: 2012/02/08, 12:30

Sample Matrix: Stack Sampling Train

# Samples Received: 10

Date Date Method

Analyses Quantity Extracted Analyzed Laboratory Method Reference

Metals B.H. in H2O2/HNO3 Imp.(6020) 10 2012/02/14 2012/02/15 BRL SOP-00103 / BRL EPA 6020 / M29 

SOP-00102

Metals F.H. in Filter + Rinses (6020) 10 2012/02/15 2012/02/15 BRL SOP-00103/ BRL EPA 6020 / M29 

SOP-00102

Particulates/Acetone Rinse (M5/315/M201) 10 2012/02/10 2012/02/15 BRL SOP-00109 EPA 5/315 

Particulates/Filter (M5/315/NJATM1/M201) 10 N/A 2012/02/15 BRL SOP-00109 EPA 5/315/NJATM1 

Final Volume of Acetone Probe Rinse 10 N/A 2012/02/13 BRL SOP-00109 

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

U = Undetected at the limit of quantitation.

J = Estimated concentration between the EDL & RDL.

B = Blank Contamination.

Q = One or more quality control criteria failed.

Encryption Key

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

CLAYTON JOHNSON, Project Manager

Email: CJohnson@maxxam.ca

Phone# (905) 817-5769

====================================================================

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 9
BT Environmental Consulting

Maxxam Job #: B218757 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN

Maxxam ID M M 1 5 8 5 M M 1 5 8 6 M M 1 5 8 7 M M 1 5 8 8

Sampling Date 2012/01/31 2012/02/01 2012/02/01 2012/02/02

 U n i t s BLANK-M5/29 RUN RUN RUN RDL QC Batch

1-122-1-M5/29 2-122-1-M5/29 3-122-1-M5/29

Acetone Rinse Particulate Weight in Acetone Rinse mg 0.5 5.8 4.3 3.4 0.5 2760823

Front Half Particulate Weight on Filter mg 0.060 U 0.060 U 0.060 U 0.060 U 0.30 2760822

Acetone Rinse Volume ml 100 83 96 93 1 2760824

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Maxxam ID M M 1 5 8 9 M M 1 5 9 0 M M 1 5 9 1 M M 1 5 9 2

Sampling Date 2012/02/01 2012/02/01 2012/02/02 2012/01/30

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

1-122-2-M5/29 2-122-2-M5/29 3-122-2-M5/29 1-123-M5/29

Acetone Rinse Particulate Weight in Acetone Rinse mg 5.0 3.6 5.1 5.4 0.5 2760823

Front Half Particulate Weight on Filter mg 0.060 U 0.060 U 0.060 U 0.060 U 0.30 2760822

Acetone Rinse Volume ml 83 90 95 94 1 2760824

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Maxxam ID M M 1 5 9 3 M M 1 5 9 4

Sampling Date 2012/01/31 2012/01/31

 U n i t s RUN RUN RDL QC Batch

2-123-M5/29 3-123-M5/29

Acetone Rinse Particulate Weight in Acetone Rinse mg 11.5 2.6 0.5 2760823

Front Half Particulate Weight on Filter mg 0.060 U 0.060 U 0.30 2760822

Acetone Rinse Volume ml 89 78 1 2760824

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Page 2 of 9
BT Environmental Consulting

Maxxam Job #: B218757 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

ELEMENTS BY ICP/MS (STACK SAMPLING TRAIN)

Maxxam ID M M 1 5 8 5 M M 1 5 8 6 M M 1 5 8 6 M M 1 5 8 7 M M 1 5 8 8

Sampling Date 2012/01/31 2012/02/01 2012/02/01 2012/02/01 2012/02/02

 U n i t s BLANK-M5/29 RDL RUN RUN RUN RUN RDL QC Batch

1-122-1-M5/29 1-122-1-M5/29 2-122-1-M5/29 3-122-1-M5/29

Lab-Dup

Back Half Chromium (Cr) ug 0.71 0.15 0.74 0.78 0.93 0.70 0.15 2764219

Front Half Chromium (Cr) ug 0.85 0.30 2.83 2.70 10.6 10.6 0.60 2765210

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Maxxam ID M M 1 5 8 9 M M 1 5 9 0 M M 1 5 9 1 M M 1 5 9 2 M M 1 5 9 3 M M 1 5 9 4

Sampling Date 2012/02/01 2012/02/01 2012/02/02 2012/01/30 2012/01/31 2012/01/31

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

1-122-2-M5/29 2-122-2-M5/29 3-122-2-M5/29 1-123-M5/29 2-123-M5/29 3-123-M5/29

Back Half Chromium (Cr) ug 0.70 0.82 0.71 1.06 0.81 0.70 0.15 2764219

Front Half Chromium (Cr) ug 2.39 1.61 1.09 1.19 1.79 1.00 0.60 2765210

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Page 3 of 9
BT Environmental Consulting

Maxxam Job #: B218757 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

Test Summary

Maxxam ID MM1585 Collected 2012/01/31

Sample ID BLANK-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Maxxam ID MM1586 Collected 2012/02/01

Sample ID RUN 1-122-1-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Maxxam ID MM1586 D u p Collected 2012/02/01

Sample ID RUN 1-122-1-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/15 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/16 2012/02/15 NAN RAYKHA

Maxxam ID MM1587 Collected 2012/02/01

Sample ID RUN 2-122-1-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Maxxam ID MM1588 Collected 2012/02/02

Sample ID RUN 3-122-1-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Page 4 of 9
BT Environmental Consulting

Maxxam Job #: B218757 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

Test Summary

Maxxam ID MM1589 Collected 2012/02/01

Sample ID RUN 1-122-2-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Maxxam ID MM1590 Collected 2012/02/01

Sample ID RUN 2-122-2-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Maxxam ID MM1591 Collected 2012/02/02

Sample ID RUN 3-122-2-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Maxxam ID MM1592 Collected 2012/01/30

Sample ID RUN 1-123-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Maxxam ID MM1593 Collected 2012/01/31

Sample ID RUN 2-123-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Page 5 of 9
BT Environmental Consulting

Maxxam Job #: B218757 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

Test Summary

Maxxam ID MM1594 Collected 2012/01/31

Sample ID RUN 3-123-M5/29 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Metals B.H. in H2O2/HNO3 Imp.(6020) ICP1/MS 2764219 2012/02/14 2012/02/15 NAN RAYKHA

Metals F.H. in Filter + Rinses (6020) ICP1/MS 2765210 2012/02/15 2012/02/15 NAN RAYKHA

Particulates/Acetone Rinse (M5/315/M201) BAL 2760823 2012/02/10 2012/02/15 BRENDA MOORE

Particulates/Filter (M5/315/NJATM1/M201) BAL 2760822 N/A 2012/02/15 BRENDA MOORE

Final Volume of Acetone Probe Rinse 2760824 N/A 2012/02/13 BRENDA MOORE

Page 6 of 9
BT Environmental Consulting

Maxxam Job #: B218757 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN

Particulates/Filter (M5/315/NJATM1/M201): Negative weights observed. See comments below.

Maxxam # Filter Condition

MM1585-01RNormal

MM1586-01RDE Pieces of filter missing

MM1587-01RLFT

MM1588-01RLFT

MM1589-01RLFT

MM1590-01RNormal

MM1591-01RLFT

MM1592-01RNormal

MM1593-01RDE Pieces of filter missing

MM1594-01RNormal

Normal Filters received in normal condition

LFT Loose filter material in the petri dish

DE Edges of the filter are frayed

ELEMENTS BY ICP/MS (STACK SAMPLING TRAIN)

Metals B.H. in H2O2/HNO3 Imp.(6020): Post digestion duplicate and spike was done on sample MM1586.

Metals F.H. in Filter + Rinses (6020): Extra 2x dilution was required for all samples except MM1585, due to the matrix

Post digestion duplicate and spike was done on sample MM1586.

Results relate only to the items tested.

Page 7 of 9
BT Environmental Consulting

Attention: James K. Sharp 

Client Project #: 11-4191.05

P.O. #: 

Site Location: JM MCPHERSON

Quality Assurance Report

Maxxam Job Number: GB218757

QA/QC Date

Batch Analyzed

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

2760823 RSU Method Blank Acetone Rinse Particulate Weight in Acetone 2012/02/15 0.1 J, MDL=0.1 mg

2764219 N_R Matrix Spike

(MM1586) Back Half Chromium (Cr) 2012/02/15 97 % 70 - 130

Matrix Spike DUP

(MM1586) Back Half Chromium (Cr) 2012/02/15 99 % 70 - 130

MS/MSD RPD Back Half Chromium (Cr) 2012/02/15 2.0 % 20

Spiked Blank Back Half Chromium (Cr) 2012/02/15 108 % 85 - 115

Spiked Blank DUP Back Half Chromium (Cr) 2012/02/15 103 % 85 - 115

RPD Back Half Chromium (Cr) 2012/02/15 4.7 % 20

Method Blank Back Half Chromium (Cr) 2012/02/15 0.070 U, MDL=0.070 ug

Method Blank DUP Back Half Chromium (Cr) 2012/02/15 0.070 U, MDL=0.070 ug

RPD Back Half Chromium (Cr) 2012/02/15 NC % 20

RPD -

Sample/Sample

Dup Back Half Chromium (Cr) 2012/02/15 NC % 20

2765210 N_R Matrix Spike

(MM1586) Front Half Chromium (Cr) 2012/02/15 102 % 70 - 130

Matrix Spike DUP

(MM1586) Front Half Chromium (Cr) 2012/02/15 100 % 70 - 130

MS/MSD RPD Front Half Chromium (Cr) 2012/02/15 2.0 % 20

Spiked Blank Front Half Chromium (Cr) 2012/02/15 98 % 85 - 115

Spiked Blank DUP Front Half Chromium (Cr) 2012/02/15 98 % 85 - 115

RPD Front Half Chromium (Cr) 2012/02/15 0.6 % 20

Method Blank Front Half Chromium (Cr) 2012/02/15 0.10 U, MDL=0.10 ug

Method Blank DUP Front Half Chromium (Cr) 2012/02/15 0.10 U, MDL=0.10 ug

RPD Front Half Chromium (Cr) 2012/02/15 NC % 20

RPD -

Sample/Sample

Dup Front Half Chromium (Cr) 2012/02/15 NC % 20

Duplicate: Paired analysis of a separate portion of the same sample. Used to evaluate the variance in the measurement.

Matrix Spike: A sample to which a known amount of the analyte of interest has been added. Used to evaluate sample matrix interference.

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.

NC (RPD): The RPD was not calculated. The level of analyte detected in the parent sample and its duplicate was not sufficiently significant to permit a

reliable calculation.

Page 8 of 9
Validation Signature Page

Maxxam Job #: B218757

The analytical data and all QC contained in this report were reviewed and validated by the following individual(s).

FRANK MO, B.Sc., Inorganic Lab. Manager 

====================================================================

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.

Page 9 of 9
Your Project #: 11-4191.05 

Site Location: JM MCPHERSON 

Attention: James K. Sharp

BT Environmental Consulting

4949 Fernlee Avenue

Royal Oak, MI

USA 48073

Report Date: 2012/02/16

CERTIFICATE OF ANALYSIS

MAXXAM JOB #: B218701

Received: 2012/02/08, 12:30

Sample Matrix: Stack Sampling Train

# Samples Received: 11

Date Date Method

Analyses Quantity Extracted Analyzed Laboratory Method Reference

Hexavalent Chromium (M0061) 11 2012/02/13 2012/02/13 BRL SOP-00106 EPA 7199 (M0061) 

Chromium on Filter by ICP 10 2012/02/14 2012/02/14 CAM SOP-00408 / BRL EPA M0061 

SOP-00102

Chromium in Impinger by ICP 11 2012/02/14 2012/02/14 CAM SOP-00408 / BRL EPA M0061 

SOP-00102

Chromium in Train Rinse by ICP 10 2012/02/14 2012/02/14 CAM SOP-00408 / BRL EPA M0061 

SOP-00102

Final Volume of KOH Impinger 11 N/A 2012/02/14 

Final Volume of Train Rinse 10 N/A 2012/02/14 

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

U = Undetected at the limit of quantitation.

J = Estimated concentration between the EDL & RDL.

B = Blank Contamination.

Q = One or more quality control criteria failed.

Encryption Key

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

CLAYTON JOHNSON, Project Manager

Email: CJohnson@maxxam.ca

Phone# (905) 817-5769

====================================================================

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 9
BT Environmental Consulting

Maxxam Job #: B218701 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN

Maxxam ID M M 1 3 8 2 M M 1 3 8 3 M M 1 3 8 4 M M 1 3 8 4

Sampling Date 2012/01/31 2012/01/31 2012/02/01 2012/02/01

 U n i t s BLANK RDL BLANK-M0061 RDL RUN RUN RDL QC Batch

H20-M0061 1-122-1-M0061 1-122-1-M0061

Lab-Dup

Potassium Hydroxide Volume ml 401 1 295 1 722 1 2760235

Rinse Volume ml 1 310 1 310 1 2763747

Hexavalent Chromium (Cr 6+) ug 0.03 U 0.2 0.4 0.1 0.31 J 0.30 J 0.4 2760223

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Maxxam ID M M 1 3 8 5 M M 1 3 8 6 M M 1 3 8 7 M M 1 3 8 8 M M 1 3 8 9

Sampling Date 2012/02/01 2012/02/02 2012/02/01 2012/02/01 2012/02/02

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

2-122-1-M0061 3-122-1-M0061 1-122-2-M0061 2-122-2-M0061 3-122-2-M0061

Potassium Hydroxide Volume ml 577 685 681 648 631 1 2760235

Rinse Volume ml 300 250 270 340 250 1 2763747

Hexavalent Chromium (Cr 6+) ug 0.19 J 0.16 J 0.5 0.21 J 0.16 J 0.3 2760223

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Maxxam ID M M 1 4 0 6 M M 1 4 0 7 M M 1 4 0 8

Sampling Date 2012/01/30 2012/01/31 2012/01/31

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

1-123-M0061 2-123-M0061 3-123-M0061

Potassium Hydroxide Volume ml 624 1 809 1 687 1 2760235

Rinse Volume ml 280 1 220 1 310 1 2763747

Hexavalent Chromium (Cr 6+) ug 0.3 0.3 0.06 U 0.4 0.3 0.3 2760223

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Page 2 of 9
BT Environmental Consulting

Maxxam Job #: B218701 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

ELEMENTS BY ICP-AES (STACK SAMPLING TRAIN)

Maxxam ID M M 1 3 8 2 M M 1 3 8 3 M M 1 3 8 4 M M 1 3 8 4 M M 1 3 8 5

Sampling Date 2012/01/31 2012/01/31 2012/02/01 2012/02/01 2012/02/01

 U n i t s BLANK BLANK-M0061 RDL RUN RUN RDL RUN RDL QC Batch

H20-M0061 1-122-1-M0061 1-122-1-M0061 2-122-1-M0061

Lab-Dup

Back Half Chromium (Cr) ug 1 U 1 U 2 2 J 2 U 4 2 U 3 2763741

Front Half Chromium (Cr) ug 0.2 U 0.3 0.2 U 0.2 U 0.3 0.2 U 0.3 2763743

Rinse Chromium (Cr) ug 1 U 2 1 U 1 U 2 1 U 2 2763744

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Maxxam ID M M 1 3 8 6 M M 1 3 8 7 M M 1 3 8 8 M M 1 3 8 9 M M 1 4 0 6

Sampling Date 2012/02/02 2012/02/01 2012/02/01 2012/02/02 2012/01/30

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

3-122-1-M0061 1-122-2-M0061 2-122-2-M0061 3-122-2-M0061 1-123-M0061

Back Half Chromium (Cr) ug 2 U 2 U 2 J 4 2 U 4 3 J 4 2763741

Front Half Chromium (Cr) ug 0.2 U 0.2 U 0.2 U 0.3 0.2 U 0.3 0.2 U 0.3 2763743

Rinse Chromium (Cr) ug 1 U 2 J 1 U 2 0.5 U 1 1 U 2 2763744

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Maxxam ID M M 1 4 0 7 M M 1 4 0 8

Sampling Date 2012/01/31 2012/01/31

 U n i t s RUN RDL RUN RDL QC Batch

2-123-M0061 3-123-M0061

Back Half Chromium (Cr) ug 3 U 5 2 U 4 2763741

Front Half Chromium (Cr) ug 0.2 U 0.3 0.2 U 0.3 2763743

Rinse Chromium (Cr) ug 0.5 U 1 1 U 2 2763744

RDL = Reportable Detection Limit

QC Batch = Quality Control Batch

Page 3 of 9
BT Environmental Consulting

Maxxam Job #: B218701 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

Test Summary

Maxxam ID MM1382 Collected 2012/01/31

Sample ID BLANK H20-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Maxxam ID MM1383 Collected 2012/01/31

Sample ID BLANK-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Maxxam ID MM1384 Collected 2012/02/01

Sample ID RUN 1-122-1-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Maxxam ID MM1384 D u p Collected 2012/02/01

Sample ID RUN 1-122-1-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Maxxam ID MM1385 Collected 2012/02/01

Sample ID RUN 2-122-1-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Page 4 of 9
BT Environmental Consulting

Maxxam Job #: B218701 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

Test Summary

Maxxam ID MM1386 Collected 2012/02/02

Sample ID RUN 3-122-1-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Maxxam ID MM1387 Collected 2012/02/01

Sample ID RUN 1-122-2-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Maxxam ID MM1388 Collected 2012/02/01

Sample ID RUN 2-122-2-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Maxxam ID MM1389 Collected 2012/02/02

Sample ID RUN 3-122-2-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Page 5 of 9
BT Environmental Consulting

Maxxam Job #: B218701 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

Test Summary

Maxxam ID MM1406 Collected 2012/01/30

Sample ID RUN 1-123-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Maxxam ID MM1407 Collected 2012/01/31

Sample ID RUN 2-123-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Maxxam ID MM1408 Collected 2012/01/31

Sample ID RUN 3-123-M0061 Shipped

Matrix Stack Sampling Train Received 2012/02/08

Test Description Instrumentation Batch Extracted Analyzed Analyst

Hexavalent Chromium (M0061) IC/SPEC 2760223 2012/02/13 2012/02/13 LANG LE

Chromium on Filter by ICP ICP 2763743 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Impinger by ICP ICP 2763741 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Chromium in Train Rinse by ICP ICP 2763744 2012/02/14 2012/02/14 SUBAN KANAPATHIPPLLAI

Final Volume of KOH Impinger 2760235 N/A 2012/02/14 FRANK MO

Final Volume of Train Rinse 2763747 N/A 2012/02/14 FRANK MO

Page 6 of 9
BT Environmental Consulting

Maxxam Job #: B218701 Client Project #: 11-4191.05

Report Date: 2012/02/16 Site Location: JM MCPHERSON

GENERAL COMMENTS

Results relate only to the items tested.

Page 7 of 9
BT Environmental Consulting

Attention: James K. Sharp 

Client Project #: 11-4191.05

P.O. #: 

Site Location: JM MCPHERSON

Quality Assurance Report

Maxxam Job Number: GB218701

QA/QC Date

Batch Analyzed

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

2760223 LLE Matrix Spike

(MM1384) Hexavalent Chromium (Cr 6+) 2012/02/13 105 % 80 - 120

Spiked Blank Hexavalent Chromium (Cr 6+) 2012/02/13 94 % 90 - 110

Method Blank Hexavalent Chromium (Cr 6+) 2012/02/13 0.03 U, MDL=0.03 ug

RPD -

Sample/Sample

Dup Hexavalent Chromium (Cr 6+) 2012/02/13 NC % 20

2763741 SUK Matrix Spike

(MM1384) Back Half Chromium (Cr) 2012/02/14 95 % 80 - 120

Matrix Spike DUP

(MM1384) Back Half Chromium (Cr) 2012/02/14 95 % 80 - 120

MS/MSD RPD Back Half Chromium (Cr) 2012/02/14 0.1 % 20

Spiked Blank Back Half Chromium (Cr) 2012/02/14 99 % 90 - 110

Spiked Blank DUP Back Half Chromium (Cr) 2012/02/14 98 % 90 - 110

RPD Back Half Chromium (Cr) 2012/02/14 1.2 % 20

Method Blank Back Half Chromium (Cr) 2012/02/14 0.3 U, MDL=0.3 ug

RPD -

Sample/Sample

Dup Back Half Chromium (Cr) 2012/02/14 NC % 20

2763743 SUK Matrix Spike

(MM1384) Front Half Chromium (Cr) 2012/02/14 101 % 80 - 120

Spiked Blank Front Half Chromium (Cr) 2012/02/14 105 % 90 - 110

Spiked Blank DUP Front Half Chromium (Cr) 2012/02/14 105 % 90 - 110

RPD Front Half Chromium (Cr) 2012/02/14 0.3 % 20

Method Blank Front Half Chromium (Cr) 2012/02/14 0.2 U, MDL=0.2 ug

RPD -

Sample/Sample

Dup Front Half Chromium (Cr) 2012/02/14 NC % 20

2763744 SUK Matrix Spike

(MM1384) Rinse Chromium (Cr) 2012/02/14 101 % 80 - 120

Matrix Spike DUP

(MM1384) Rinse Chromium (Cr) 2012/02/14 101 % 80 - 120

MS/MSD RPD Rinse Chromium (Cr) 2012/02/14 0.5 % 20

Spiked Blank Rinse Chromium (Cr) 2012/02/14 98 % 90 - 110

Spiked Blank DUP Rinse Chromium (Cr) 2012/02/14 98 % 90 - 110

RPD Rinse Chromium (Cr) 2012/02/14 1.0 % 20

Method Blank Rinse Chromium (Cr) 2012/02/14 0.3 U, MDL=0.3 ug

RPD -

Sample/Sample

Dup Rinse Chromium (Cr) 2012/02/14 NC % 20

Duplicate: Paired analysis of a separate portion of the same sample. Used to evaluate the variance in the measurement.

Matrix Spike: A sample to which a known amount of the analyte of interest has been added. Used to evaluate sample matrix interference.

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.

NC (RPD): The RPD was not calculated. The level of analyte detected in the parent sample and its duplicate was not sufficiently significant to permit a

reliable calculation.

Page 8 of 9
Validation Signature Page

Maxxam Job #: B218701

The analytical data and all QC contained in this report were reviewed and validated by the following individual(s).

FRANK MO, B.Sc., Inorganic Lab. Manager 

====================================================================

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.

Page 9 of 9
Acetone 

Rinse 

Volume 

(mL)

Particulate 

Weight in 

Acetone 

Rinse (mg)

Particulate 

Weight on 

Filter (mg)

Particulate 

Weight in 

Acetone 

Rinse (mg)

Combined 

Particulate 

Weight (mg)

Run 1 83 5.8 0.06 5.4 5.7

Run 2 96 4.3 0.06 3.8 4.1

Run 3 93 3.4 0.06 2.9 3.2

Blank 100 0.5 0.06

Note: Run detection limits of 0.3 mg in the acetone rinse were used in placeof the corrected values listed above

Method 5 PM Lab Results line 122-1

Corrected

Sampling Date: January 23 and 26, 2012

BTEC job #11-4191.03

McPherson

Johns Manville
Compound/Fraction

Blank 

Filter 

Result

(μg)

Blank 

Filter 

Detection 

Limit

(μg)

Run 1 

Result

(μg)

Run 2 

Result

(μg)

Run 3 

Result

(μg)

Test Run 

Detection 

Limit

(μg)

Run 1

(μg)

Ru

(μ

Back Half Chromium (Vaporous) 0.71 0.15 0.74 0.93 0.7 0.15 0.15 0

Front Half Chromium (Filterable) 0.85 0.30 2.83 10.6 10.6 0.60 1.98 9

Note: For Runs 1 and 3, the test run detection limit of 0.15 μg was used for the back half result.

Johns Manville

Method 29 Lab Results line 122-1

Corr

Sampling Date: January 23 and 26, 2012

BTEC job #11-4191.03

McPherson
Corrected

Total Volume 

(ml)

Impinger KOH 

(ml)

Hexavalent 

Chromium, 

Cr6+ [μg] RDL

Hexavalent 

Chromium, 

Cr6+ [μg]

Run 1 1032 722 0.31 0.40 0.40

Run 2 877 577 0.19 0.30 0.30

Run 3 935 685 0.16 0.30 0.30

Blank KOH 605 0.40 0.10

Note: No blank correction applied. RDL used to calculate results.

Total Volume 

(ml)

Impinger KOH 

(ml)

Back Half 

Chromium 

(μg)

Back Half 

RDL

Front Half 

Chromium 

(μg)

Front Half 

RDL

Rinse 

Chromium 

(μg)

Run 1 1032 722 2.00 4.00 0.20 0.30 1.00 

Run 2 877 577 2.00 3.00 0.20 0.30 1.00 Run 3 935 685 2.00 4.00 0.20 0.30 1.00 

Blank KOH 605 1.00 2.00 0.20 0.30 1.00 

Note: No blank correction applied. RDL used for all fractions.

Method 0061 Lab Results line 122-1

Sampling Date: January 23 and 26, 2012

BTEC job #11-4191.03

McPherson

Johns Manville
Acetone 

Rinse 

Volume 

(mL)

Particulate 

Weight in 

Acetone 

Rinse (mg)

Particulate 

Weight on 

Filter (mg)

Particulate 

Weight in 

Acetone 

Rinse (mg)

Combined 

Particulate 

Weight (mg)

Run 1 83 5.0 0.06 4.6 4.9

Run 2 90 3.6 0.06 3.2 3.5

Run 3 95 5.1 0.06 4.6 4.9

Blank 100 0.5 0.06

Note: Run detection limits of 0.3 mg in the acetone rinse were used in placeof the corrected values listed above

Method 5 PM Lab Results Line 122-2

Corrected

Sampling Date: January 30-February 2, 2012

BTEC job #11-4191.04

McPherson, Kansas

Johns Manville
Compound/Fraction

Blank 

Filter 

Result

(μg)

Blank 

Filter 

Detection 

Limit

(μg)

Run 1 

Result

(μg)

Run 2 

Result

(μg)

Run 3 

Result

(μg)

Test Run 

Detection 

Limit

(μg)

Run 1

(μg)

Ru

(μ

Back Half Chromium (Vaporous) 0.71 0.15 0.7 0.82 0.71 0.15 0.15 0

Front Half Chromium (Filterable) 0.85 0.30 2.39 1.61 1.09 0.60 1.54 0

Note: The test run detection limit of 0.15 μg was used for the back half result and 0.60 μg was used for the front half result fo

Johns Manville

Method 29 Lab Results Line 122-2

Corr

Sampling Date: January 30-February 2, 2012

BTEC job #11-4191.04

McPherson, Kansas
Corrected

Total Volume 

(ml)

Impinger KOH 

(ml)

Hexavalent 

Chromium, 

Cr6+ [μg] RDL

Hexavalent 

Chromium, 

Cr6+ [μg]

Run 1 851 681 0.50 0.30 0.30

Run 2 988 648 0.21 0.30 0.30

Run 3 881 631 0.16 0.30 0.30

Blank KOH 605 0.40 0.10

Note: No blank correction applied. RDL used to calculate results.

Total Volume 

(ml)

Impinger KOH 

(ml)

Back Half 

Chromium 

(μg)

Back Half 

RDL

Front Half 

Chromium 

(μg)

Front Half 

RDL

Rinse 

Chromium 

(μg)

Run 1 851 681 2.00 4.00 0.20 0.30 2.00 

Run 2 988 648 2.00 4.00 0.20 0.30 1.00 Run 3 881 631 2.00 4.00 0.20 0.30 0.50 

Blank KOH 605 1.00 2.00 0.20 0.30 1.00 

Note: No blank correction applied. RDL used for all fractions.

Method 0061 Lab Results Line 122-2

Sampling Date: January 30-February 2, 2012

BTEC job #11-4191.04

McPherson, Kansas

Johns Manville
Acetone 

Rinse 

Volume 

(mL)

Particulate 

Weight in 

Acetone 

Rinse (mg)

Particulate 

Weight on 

Filter (mg)

Particulate 

Weight in 

Acetone 

Rinse (mg)

Combined 

Particulate 

Weight (mg)

Run 1 94 5.4 0.06 4.9 5.2

Run 2 89 11.5 0.06 11.1 11.4

Run 3 78 2.6 0.06 2.2 2.5

Blank 100 0.5 0.06

Note: Run detection limits of 0.3 mg in the acetone rinse were used in placeof the corrected values listed above

Method 5 PM Lab Results Line 123

Corrected

Sampling Date: January 30-February 2, 2012

BTEC job #11-4191.04

McPherson, Kansas

Johns Manville
Compound/Fraction

Blank 

Filter 

Result

(μg)

Blank 

Filter 

Detection 

Limit

(μg)

Run 1 

Result

(μg)

Run 2 

Result

(μg)

Run 3 

Result

(μg)

Test Run 

Detection 

Limit

(μg)

Run 1

(μg)

Ru

(μ

Back Half Chromium (Vaporous) 0.71 0.15 1.06 0.81 0.7 0.15 0.35 0

Front Half Chromium (Filterable) 0.85 0.30 1.09 1.79 1 0.60 0.60 0

Note: For Runs 2 and 3, the test run detection limit of 0.15 μg was used for the back half result 

and 0.60 μg was used for the front half for Run 1 and 3.

Johns Manville

Method 29 Lab Results Line 123

Corr

Sampling Date: January 30-February 2, 2012

BTEC job #11-4191.04

McPherson, Kansas
Corrected

Total Volume 

(ml)

Impinger KOH 

(ml)

Hexavalent 

Chromium, 

Cr6+ [μg] RDL

Hexavalent 

Chromium, 

Cr6+ [μg]

Run 1 904 624 0.30 0.30 0.30

Run 2 1029 809 0.06 0.40 0.40

Run 3 997 687 0.30 0.30 0.30

Blank KOH 605 0.40 0.10

Note: No blank correction applied. RDL used to calculate results.

Total Volume 

(ml)

Impinger KOH 

(ml)

Back Half 

Chromium 

(μg)

Back Half 

RDL

Front Half 

Chromium 

(μg)

Front Half 

RDL

Rinse 

Chromium 

(μg)

Run 1 904 624 3.00 4.00 0.20 0.30 1.00 

Run 2 1029 809 3.00 5.00 0.20 0.30 0.50 Run 3 997 687 2.00 4.00 0.20 0.30 1.00 

Blank KOH 605 1.00 2.00 0.20 0.30 1.00 

Note: No blank correction applied. RDL used for all fractions.

Method 0061 Lab Results Line 123

Sampling Date: January 30-February 2, 2012

BTEC job #11-4191.04

McPherson, Kansas

Johns Manville