EMISSIONS TEST REPORT 

FELMAN PRODUCTION, INC. 

FURNACE #2 BAGHOUSE (ID# 001-01) 

WVDEP DAQ PERMIT # R30-0530004-2007 

PLANT ID# 03-54-05300004 

LETART, WEST VIRGINIA 

MARCH2013 

TI-1550 

~~·TEST, Inc. • www.testincorp.com 

Technical Environmental Services Team 

Route 2, Box 33-B, Poca, West Virginia 25159 Ph: (304) 755-1077 Fx: (304) 755-1099 
TABLE OF CONTENTS 

Introduction 

Summary of Results 

Discussion of Results 

Sampling and Analytical Procedures 

Sampling Location 

Appendixes 

A - Computer Data and Example Calculations 

B -Pre-flow Data 

C- Analytical Data 

D - Field Data Sheets 

E- Calibration Data 

F - Chain of Custody 

List of Tables 

Table 1 Summary of Results HCl 

Table 2 Summary of Results Particulate Matter 

Table 2a Summary of Results Metals 

Table 3 Summary of Results Mercury 

Table 4 Dioxins/Furans/PCBs Sampling Data 

Table 4a Summary of Results PCBs 

Table 4b Summary ofResults PCBs (cont.) 

Table 4c Summary ofResults PCBs (cont.) 

Table 4d Summary ofResults PCBs (cont.) 

Table 4e Summary of Results Dioxins 

Table 4f Summary of Results Dioxins (cont.) 

Table 4g Summary of Results Furans 

Table 4h Summary of Results Furans (cont.) 

Table 5 P AHs Sampling Data 

Table 5a Summary of Results P AHs 

Table 5b Summary of Results PAHs (cont.) 

Table 5c Summary of Results PAHs (cont.) 

Table 5d Summary of Results P AHs (cont.) 

1 

1 

20 

22 

27 

29 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

13 

14 

15 

16 

17 

18 

19 
INTRODUCTION 

Emissions Test Report 

Felman Production, Inc. 

Furnace #2 Baghouse (ID#OO 1-01) 

WVDEP DAQ Permit# R30-0530004-2007 

Plant ID# 03-54-05300004 

Letart, West Virginia 

TI-1550 

Emission testing was conducted at Felman Production, Inc. located in Letart, West Virginia on 

March 18, 19, and 20, 2013, by TEST, Incorporated, Charleston, West Virginia, under the 

direction of Paul Chinuntdet. The purpose of these tests was to determine the concentrations of 

particulate matter, hydrogen chloride, arsenic, cadmium, chromium, lead, manganese, nickel, 

mercury, dioxins/furans, polychlorinated biphenyls, and polycyclic aromatic hydrocarbons being 

emitted into the atmosphere via the Furnace #2 Baghouse. Mr. John Konrady of Felman 

Productions, LLC. coordinated the testing with plant operations. 

The testing followed the procedures in the Appendix to the Code of Federal Regulations, Title 

40, Chapter 1, Part 60, Methods 1, 2, 3A, 4, 5d, 26A, 29, and 30B; and California Air Resources 

Board Methods 428 (CARB 428), and 429 (CARB 429). 

SUMMARY OF RESULTS 

The following tables and graphs provide results for the emission rates measured on the Furnace #2 

Baghouse. The emission results are presented in micrograms per dry standard cubic meter 

(ug/dscm), nanograms per dry standard cubic meter (ng/dscm), pounds per hour (lbs/hr), and 

pounds per ton product (lbs/ton). The lbs/ton were calculated using the following production rates: 

March 18,2013 = 7.17 tons/hr, March 19,2013 = 8.38 tons/hr, and March 20,2013 = 8.87 tons/hr. 
SUMMARY OF RESULTS 

Table 1 

HCl Sampling Data 

Baghouse #2 

Run Number 1 2 

Date 3/19/13 3/19/13 

Time 855 - 1110 1215 - 1425 

Carbon Dioxide Cone. - % Vol. 0.40 0.40 

Oxygen Concentration - %Vol. 20.40 20.50 

Stack Pressure - "Hg 29.06 29.05 

Area of Stack- Sq. in. 950,400.00 950,400.00 

Volume Dry Gas Sampled - dscf 103.659 102.137 

Volume Dry Gas Sampled - dscm 2.935 2.892 

Stack Temperature - Deg. F 150.30 147.20 

Percent Moisture - % 1.39 0.50 

Velocity in the Stack - FPS 1.35 1.30 

Volumetric Flow Rate- ACFM 534,600 532,620 

Volumetric Flow Rate - DSCFM 442,970 447,432 

Isokinetic Sampling Rate - % 104.9 102.3 

Hydrogen Chloride Concentrations - ug 3100.00 2500.00 

Hydrogen Chloride Emissions - ug/dscm 1056.22 864.45 

Hydrogen Chloride Emissions - ppm 0.70 0.57 

Hydrogen Chloride Emissions - lbs/hr 1.753 1.449 

Hydrogen Chloride Emissions - lbs/ton prod. 0.209 0.173 

Production Rate (tons/hr) = 8.38 

2 

3 Average 

3/19/13 ----

1600 - 1815 ----

0.50 ----

20.40 ----

29.06 ----

950,400.00 ----

101.876 ----

2.885 ----

157.10 ----

0.62 ----

1.40 ----

537,240 ----

443,690 ----

102.9 ----

1900.00 2500.00 

658.58 859.75 

0.43 0.57 

1.095 1.432 

0.131 0.171 
SUMMARY OF RESULTS 

Table 2 

Particulate/Metals Sampling Data 

Baghouse #2 

Run Number 1 2 

Date 3/20/13 3/20113 

Time 900- 1315 900- 1315 

Carbon Dioxide Cone. - % Vol. 0.40 0.40 

Oxygen Concentration - %Vol. 20.40 20.40 

Stack Pressure - "Hg 29.16 29.16 

Area of Stack - Sq. in. 950,400.00 950,400.00 

Volume Dry Gas Sampled - dscf 209.472 204.748 

Volume Dry Gas Sampled - dscm 5.932 5.798 

Stack Temperature - Deg. F 145.10 153.20 

Percent Moisture - % 0.40 0.62 

Velocity in the Stack - FPS 1.34 1.40 

Volumetric Flow Rate - ACFM 530,640 534,600 

Volumetric Flow Rate - DSCFM 449,461 445,847 

Isokinetic Sampling Rate - % 104.4 102.9 

Particulate Matter Concentrations- gr/acf 0.0003 0.0003 

Particulate Matter Concentrations- gr/dscf 0.0004 0.0003 

Particulate Matter Concentrations- ug/dscm 859.74 730.14 

Particulate Matter Emissions - lbs/hr 1.54 1.15 

Particulate Matter Emissions - lbs/ton prod. 0.17 0.13 

Production Rate (tons/hr) = 8.87 

3 

3 Average 

3/20113 ----

1440 - 1850 ----

0.40 ----

20.50 ----

29.06 ----

950,400.00 ----

213.968 ----

6.059 ----

142.50 ----

0.50 ----

1.30 ----

530,640 ----

449,401 ----

106.7 ----

0.0003 0.0003 

0.0003 0.0003 

792.21 794.03 

1.16 1.28 

0.13 0.14 
SUMMARY OF RESULTS 

Table 2a 

Particulate/Metals Sampling Data 

Baghouse #2 

Run Number 1 2 

Arsenic Concentrations - ug 2.0 2.0 

Arsenic Emissions- ug/dscm 0.34 0.34 

Arsenic Emissions - lbslhr 0.0006 0.0006 

Arsenic Emissions - lbs/ton prod. 0.0001 0.0001 

Cadmium Concentrations - ug 0.50 0.50 

Cadmium Emissions - ug/dscm 0.08 0.09 

Cadmium Emissions - lbslhr 0.0001 0.0001 

Cadmium Emissions -lbs/ton prod. 1.60E-05 1.62E-05 

Chromium Concentrations - ug 3.90 11.40 

Chromium Emissions- ug/dscm 0.66 1.97 

Chromium Emissions -lbslhr 0.0011 0.0033 

Chromium Emissions - lbs/ton prod. 0.0001 0.0004 

Lead Concentrations- ug 50.00 25.00 

Lead Emissions - ug/dscm 8.43 4.31 

Lead Emissions -lbslhr 0.0142 0.0072 

Lead Emissions - lbs/ton prod. 0.0016 0.0008 

Manganese Concentrations- ug 3370.00 976.00 

Manganese Emissions - ug/dscm 568.11 168.33 

Manganese Emissions - lbslhr 0.9567 0.2812 

Manganese Emissions - lbs/ton prod. 0.1079 0.0317 

Nickel Concentrations- ug 4.70 11.10 

Nickel Emissions- ug/dscm 0.79 1.91 

Nickel Emissions - lbslhr 0.0013 0.0032 

Nickel Emissions - lbs/ton prod. 0.0002 0.0004 

Production Rate (tonslhr) = 8.87 

3 Average 

2.0 2.0 

0.33 0.34 

0.0006 0.0006 

0.0001 0.0001 

0.50 0.50 

0.08 0.08 

0.0001 0.0001 

1.57E-05 1.60E-05 

6.50 7.27 

1.07 1.23 

0.0018 0.0021 

0.0002 0.0002 

28.30 34.43 

4.67 5.80 

0.0079 0.0098 

0.0009 0.0011 

1280.00 1875.33 

211.26 315.90 

0.3557 0.5312 

0.0401 0.0599 

9.10 8.30 

1.50 1.40 

0.0025 0.0024 

0.0003 0.0003 
Vl 

SUMMARY OF RESULTS 

Time Run Trap 

1128 - 1328 1 A 156034 

B 156058 

Average 

% Relative Deviation 

Time Run Trap 

1355 - 1555 2 A 156069 

B 150824 

Average 

% Relative Deviation 

Time Run Trap 

1615 - 1815 3 A 156006 

B 156057 

Average 

% Relative Deviation 

* Spiked 

Production Rate (tons/hr) = 7.17 

Table 3 

Vapor Stage Mercury Test Results 

Baghouse 2 

Sample Sample 

Volume Volume Flow 

(1) (dscm) (dscfm) ug 

50.177 0.050 397,005 0.0200 

50.562 0.051 397,005 0.0180 

50.370 0.050 397,005 0.0190 

Sample Sample 

Volume Volume Flow 

(1) (dscm) (dscfm) ug 

51.755 0.052 394,798 0.0232 

52.627 0.053 394,798 0.0257 

52.191 0.052 394,798 0.0244 

Sample Sample 

Volume Volume Flow 

(1) (dscm) (dscfm) ug 

52.902 0.053 392,228 0.0291 

52.971 0.053 392,228 0.0268 

52.937 0.053 392,228 0.0279 

Mercury 

Emissions 

ug/dscm lbslhr lbs/ton prod. 

0.40 5.94E-04 8.28E-05 

0.36 5.29E-04 7.38E-05 

0.38 5.62E-04 7.83E-05 

5.72 

Mercury 

Emissions 

ug/dscm lbslhr lbs/ton prod. 

0.45 6.64E-04 9.26E-05 

0.49 7.21E-04 1.01E-04 

0.47 6.93E-04 9.66E-05 

4.14 

Mercury 

Emissions 

ug/dscm lbslhr lbs/ton prod. 

0.55 8.08E-04 1.13E-04 

0.51 7.43E-04 1.04E-04 

0.53 7.75E-04 1.08E-04 

4.20 
SUMMARY OF RESULTS 

Table 4 

Dioxin/Furans/PCB's Sampling Data 

Baghouse #2 

Run Number 1 2 

Date 3/19/13 3/19/13 

Time 855 - 1105 1220 - 1435 

Carbon Dioxide Cone. - % Vol. 0.40 0.40 

Oxygen Concentration- %Vol. 20.40 20.50 

Stack Pressure- "Hg 29.06 29.06 

Area of Stack- Sq. in. 950,400.00 950,400.00 

Volume Dry Gas Sampled - dscf 102.868 100.981 

Volume Dry Gas Sampled - dscm 2.913 2.859 

Stack Temperature- Deg. F 161.50 147.60 

Percent Moisture - % 0.89 0.76 

Velocity in the Stack - FPS 1.36 1.30 

Volumetric Flow Rate- ACFM 539,220 533,280 

Volumetric Flow Rate - DSCFM 440,971 446,676 

Isokinetic Sampling Rate - % 104.6 101.3 

6 

3 

3/19/13 

1555 - 1810 

0.50 

20.40 

29.06 

950,400.00 

104.844 

2.969 

165.00 

0.79 

1.40 

540,540 

440,019 

106.8 
Run Number 

33'44'-TetraCB-(77) 

344'5-TetraCB-(81) 

233'44'-PentaCB-(1 05) 

2344'5-PentaCB-(114) 

23'44'5-PentaCB-(118) 

23'44'5'-PentaCB-(123) 

SUMMARY OF RESULTS 

Table 4a 

PCB Sampling Data 

Baghouse #2 

1 2 

ng 4.3 2.6 

ng/dscm 1.48 0.91 

lbs/hr 2.44E-06 1.52E-06 

lbs/ton 2.91E-07 1.82E-07 

ng 0.26 0.15 

ng/dscm 0.09 0.05 

lbs/hr 1.47E-07 8.78E-08 

lbs/ton 1.76E-08 1.05E-08 

ng 4.4 2.5 

ng/dscm 1.51 0.87 

lbs/hr 2.50E-06 1.46E-06 

lbs/ton 2.98E-07 1.75E-07 

ng 0.36 0.2 

ng/dscm 0.12 0.07 

lbs/hr 2.04E-07 1.17E-07 

lbs/ton 2.44E-08 1.40E-08 

ng 12 6.7 

ng/dscm 4.12 2.34 

lbs/hr 6.81E-06 3.92E-06 

lbs/ton 8.12E-07 4.68E-07 

ng 0.23 0.11 

ng/dscm 0.08 0.04 

lbs/hr 1.30E-07 6.44E-08 

lbs/ton 1.56E-08 7.68E-09 

Production Rate (tons/hr) = 8.38 

3 Average 

1.5 2.8 

0.51 0.96 

8.33E-07 1.60E-06 

9.94E-08 1.91E-07 

0.085 0.17 

0.03 0.06 

4.72E-08 9.41E-08 

5.63E-09 1.12E-08 

1.4 2.8 

0.47 0.95 

7.77E-07 1.58E-06 

9.28E-08 1.88E-07 

0.12 0.23 

0.04 0.08 

6.66E-08 1.29E-07 

7.95E-09 1.54E-08 

3.9 8 

1.31 2.59 

2.17E-06 4.30E-06 

2.58E-07 5.13E-07 

0.082 0.14 

0.03 0.05 

4.55E-08 8.01E-08 

5.43E-09 9.56E-09 
SUMMARY OF RESULTS 

Run Number 

33'44'5-PentaCB-(126) 

HexaCB-(156)+(157) 

23'44'55'-HexaCB-(167) 

33'44'55'-HexaCB-(169) 

233'44'55'-HeptaCB-(189) 

C 13-233'44'55'-HeptaCB-(189) 

Table 4b 

PCB Sampling Data 

Baghouse #2 

1 2 

ng 0.081 0.048 

ng/dscm 0.03 0.02 

lbslhr 4.59E-08 2.81E-08 

lbs/ton 5.48E-09 3.35E-09 

ng 0.46 0.25 

ng/dscm 0.16 0.09 

lbs/hr 2.61E-07 1.46E-07 

lbs/ton 3.11E-08 1.75E-08 

ng 0.18 0.11 

ng/dscm 0.06 0.04 

lbslhr 1.02E-07 6.44E-08 

lbs/ton 1.22E-08 7.68E-09 

ng 0.033 0.037 

ng/dscm 0.01 0.01 

lbslhr 1.87E-08 2.17E-08 

lbs/ton 2.23E-09 2.58E-09 

ng 0.028 0.023 

ng/dscm 0.01 0.01 

lbs/hr 1.59E-08 1.35E-08 

lbs/ton 1.89E-09 1.61E-09 

ng 95 97 

ng/dscm 32.61 33.93 

lbslhr 5.39E-05 5.68E-05 

lbs/ton 6.43E-06 6.77E-06 

Production Rate (tonslhr) = 8.38 

3 Average 

0.033 0.05 

0.01 0.02 

1.83E-08 3.08E-08 

2.19E-09 3.67E-09 

0.17 0.29 

0.06 0.10 

9.44E-08 1.67E-07 

1.13E-08 2.00E-08 

0.068 0.12 

0.02 0.04 

3.78E-08 6.81E-08 

4.51E-09 8.12E-09 

0.039 0.04 

0.01 0.01 

2.17E-08 2.07E-08 

2.58E-09 2.47E-09 

0.023 0.02 

0.01 0.01 

1.28E-08 1.40E-08 

1.52E-09 1.68E-09 

94 95 

31.66 32.73 

5.22E-05 5.43E-05 

6.23E-06 6.48E-06 
SUMMARY OF RESULTS 

Run Number 

C13-233'44'5-HexaCB-(156) 

C 13-233'44'5'-HexaCB-(157) 

C 13-233'44'-PentaCB-(1 05) 

C13-23'44'55'-HexaCB-(167) 

CB-2344'5-PentaCB-(114) 

C13-23'44'5-PentaCB-(118) 

Table 4c 

PCB Sampling Data 

Baghouse #2 

1 2 

ng 109 110 

ng/dscm 37.42 38.47 

lbs/hr 6.18E-05 6.44E-05 

lbs/ton 7.38E-06 7.68E-06 

ng 109 110 

ng/dscm 37.42 38.47 

lbs/hr 6.18E-05 6.44E-05 

lbs/ton 7.38E-06 7.68E-06 

ng 114 113 

ng/dscm 39.13 39.52 

lbs/hr 6.47E-05 6.61E-05 

lbs/ton 7.72E-06 7.89E-06 

ng 107 106 

ng/dscm 36.73 37.08 

lbs/hr 6.07E-05 6.20E-05 

lbs/ton 7.24E-06 7.40E-06 

ng 118 113 

ng/dscm 40.51 39.52 

lbs/hr 6.69E-05 6.61E-05 

lbs/ton 7.99E-06 7.89E-06 

ng 116 113 

ng/dscm 39.82 39.52 

lbs/hr 6.58E-05 6.61E-05 

lbs/ton 7.85E-06 7.89E-06 

Production Rate (tons/hr) = 8.38 

3 Average 

102 107 

34.36 36.75 

5.66E-05 6.09E-05 

6.76E-06 7.27E-06 

102 107 

34.36 36.75 

5.66E-05 6.09E-05 

6.76E-06 7.27E-06 

109 112 

36.71 38.46 

6.05E-05 6.38E-05 

7.22E-06 7.61E-06 

100 104 

33.68 35.83 

5.55E-05 5.94E-05 

6.63E-06 7.09E-06 

106 112 

35.70 38.58 

5.89E-05 6.40E-05 

7.02E-06 7.63E-06 

105 Ill 

35.37 38.24 

5.83E-05 6.34E-05 

6.96E-06 7.57E-06 
SUMMARY OF RESULTS 

Run Number 

C13-2'344'5-PentaCB-(123) 

C 13-33'44'55'-HexaCB-(169) 

C13-33'44'5-PentaCB-(126) 

C13-33'44'-TetraCB-(77) 

C 13-344'5-TetraCB-(81) 

Table 4d 

PCB Sampling Data 

Baghouse #2 

1 2 

ng 115 111 

ng/dscm 39.48 38.82 

lbslhr 6.52E-05 6.50E-05 

lbs/ton 7.78E-06 7.75E-06 

ng 106 106 

ng/dscm 36.39 37.08 

lbslhr 6.01E-05 6.20E-05 

lbs/ton 7.17E-06 7.40E-06 

ng 117 117 

ng/dscm 40.16 40.92 

lbs/hr 6.64E-05 6.85E-05 

lbs/ton 7.92E-06 8.17E-06 

ng 121 115 

ng/dscm 41.54 40.22 

lbslhr 6.86E-05 6.73E-05 

lbs/ton 8.19E-06 8.03E-06 

ng 115 115 

ng/dscm 39.48 40.22 

lbs/hr 6.52E-05 6.73E-05 

lbs/ton 7.78E-06 8.03E-06 

Production Rate (tonslhr) = 8.38 

10 

3 Average 

103 110 

34.69 37.66 

5.72E-05 6.25E-05 

6.82E-06 7.45E-06 

90 101 

30.31 34.59 

5.00E-05 5.74E-05 

5.96E-06 6.85E-06 

113 116 

38.06 39.72 

6.27E-05 6.59E-05 

7.49E-06 7.86E-06 

110 115 

37.05 39.60 

6.11E-05 6.57E-05 

7.29E-06 7.84E-06 

111 114 

37.39 39.03 

6.16E-05 6.47E-05 

7.35E-06 7.72E-06 
Run Number 

2,3,7,8-Tetra CDD * 

1,2,3,7,8-Penta CDD 

1,2,3,4,7,8-Hexa CDD 

1,2,3,6,7,8-Hexa CDD 

1,2,3,7,8,9-Hexa CDD 

SUMMARY OF RESULTS 

Table 4e 

Dioxins Sampling Data 

Baghouse #2 

1 2 

ng 3.3 3.7 

ng/dscm 1.13 1.29 

lbslhr 1.87E-06 2.17E-06 

lbs/ton 2.23E-07 2.58E-07 

ng 3.5 3.6 

ng/dscm 1.20 1.26 

lbslhr 1.98E-06 2.11E-06 

lbs/ton 2.37E-07 2.51E-07 

ng 4.9 3.6 

ng/dscm 1.68 1.26 

lbslhr 2.78E-06 2.11E-06 

lbs/ton 3.32E-07 2.51E-07 

ng 4.8 3.4 

ng/dscm 1.65 1.19 

lbslhr 2.72E-06 1.99E-06 

lbs/ton 3.25E-07 2.37E-07 

ng 4.8 3.5 

ng/dscm 1.65 1.22 

lbs/hr 2.72E-06 2.05E-06 

lbs/ton 3.25E-07 2.44E-07 

Production Rate (tonslhr) = 8.38 

11 

3 Average 

4.1 3.7 

1.38 1.27 

2.28E-06 2.10E-06 

2.72E-07 2.51E-07 

4.1 3.7 

1.38 1.28 

2.28E-06 2.12E-06 

2.72E-07 2.53E-07 

3.9 4.1 

1.31 1.42 

2.17E-06 2.35E-06 

2.58E-07 2.80E-07 

3.8 4.0 

1.28 1.37 

2.11E-06 2.27E-06 

2.52E-07 2.71E-07 

3.8 4.0 

1.28 1.38 

2.11E-06 2.29E-06 

2.52E-07 2.74E-07 
Run Number 

1,2,3,4,6,7,8-Hepta CDD 

1,2,3,4,6,7,8,9-0cta CDD 

SUMMARY OF RESULTS 

Table 4f 

Dioxins Sampling Data 

Baghouse #2 

1 2 

ng 15.8 3.5 

ng/dscm 5.42 1.22 

1bslhr 8.96E-06 2.05E-06 

lbs/ton 1.07E-06 2.44E-07 

ng 30.4 12.3 

ng/dscm 10.44 4.30 

lbslhr 1.72E-05 7.20E-06 

lbs/ton 2.06E-06 8.59E-07 

Production Rate (tonslhr) = 8.38 

12 

3 Average 

3.2 7.5 

1.08 2.58 

1.78E-06 4.26E-06 

2.12E-07 5.09E-07 

7.7 16.8 

2.59 5.78 

4.28E-06 9.57E-06 

5.10E-07 1.14E-06 
Run Number 

2,3,7,8-Tetra CDF ** 

1,2,3,7,8-Penta CDF 

2,3,4,7,8-Penta CDF 

1,2,3,4,7,8-Hexa CDF 

1,2,3,6,7,8-Hexa CDF 

SUMMARY OF RESULTS 

Table 4g 

Furans Sampling Data 

Baghouse #2 

1 2 

ng 190 53 

ng/dscm 65.22 18.54 

lbs/hr 1.08E-04 3.10E-05 

lbs/ton 1.29E-05 3.70E-06 

ng 21.2 5.9 

ng/dscm 7.28 2.06 

lbs/hr 1.20E-05 3.45E-06 

lbs/ton 1.43E-06 4.12E-07 

ng 23.4 6 

ng/dscm 8.03 2.10 

lbs/hr 1.33E-05 3.51E-06 

lbs/ton 1.58E-06 4.19E-07 

ng 33.3 8 

ng/dscm 11.43 2.80 

lbs/hr 1.89E-05 4.68E-06 

lbs/ton 2.25E-06 5.59E-07 

ng 15.1 3.2 

ng/dscm 5.18 1.12 

lbs/hr 8.56E-06 1.87E-06 

lbs/ton 1.02E-06 2.23E-07 

Production Rate (tons/hr) = 8.38 

13 

3 Average 

78 107 

26.27 36.68 

4.33E-05 6.07E-05 

5.17E-06 7.24E-06 

9.7 12.3 

3.27 4.20 

5.39E-06 6.95E-06 

6.43E-07 8.30E-07 

12.6 14.0 

4.24 4.79 

7.00E-06 7.93E-06 

8.35E-07 9.46E-07 

13 18.1 

4.38 6.20 

7.22E-06 1.03E-05 

8.61E-07 1.22E-06 

5.2 7.8 

1.75 2.68 

2.89E-06 4.44E-06 

3.45E-07 5.30E-07 
Run Number 

2,3,4,6,7,8-Hexa CDF 

1,2,3,7,8,9-Hexa CDF 

1,2,3,4,6,7,8-Hepta CDF 

1,2,3,4,7,8,9-Hepta CDF 

1,2,3,4,6,7,8,9-0cta CDF 

SUMMARY OF RESULTS 

Table 4h 

Furans Sampling Data 

Baghouse #2 

1 2 

ng 12.2 4.1 

ng/dscm 4.19 1.43 

lbslhr 6.92E-06 2.40E-06 

lbs/ton 8.26E-07 2.86E-07 

ng 4.4 4.5 

ng/dscm 1.51 1.57 

lbslhr 2.50E-06 2.63E-06 

lbs/ton 2.98E-07 3.14E-07 

ng 25.7 5.9 

ng/dscm 8.82 2.06 

lbslhr 1.46E-05 3.45E-06 

lbs/ton 1.74E-06 4.12E-07 

ng 4.6 3.1 

ng/dscm 1.58 1.08 

lbslhr 2.61E-06 1.81E-06 

lbs/ton 3.11E-07 2.16E-07 

ng 16.1 5.3 

ng/dscm 5.53 1.85 

lbs/hr 9.13E-06 3.10E-06 

lbs/ton 1.09E-06 3.70E-07 

Production Rate (tons/hr) = 8.38 

14 

3 Average 

4.1 6.800 

1.38 2.33 

2.28E-06 3.86E-06 

2.72E-07 4.61E-07 

4.5 4.467 

1.52 1.53 

2.50E-06 2.54E-06 

2.98E-07 3.03E-07 

7.2 12.9 

2.43 4.44 

4.00E-06 7.34E-06 

4.77E-07 8.76E-07 

4 3.9 

1.35 1.34 

2.22E-06 2.21E-06 

2.65E-07 2.64E-07 

5.3 8.9 

1.79 3.06 

2.94E-06 5.06E-06 

3.51E-07 6.04E-07 
SUMMARY OF RESULTS 

Table 5 

PAH Sampling Data 

Baghouse #2 

Run Number 1 

Date 3/18113 

Time 955 - 1225 

Carbon Dioxide Cone. - % Vol. 0.40 

Oxygen Concentration - %Vol. 20.40 

Stack Pressure - "Hg 28.96 

Area of Stack - Sq. in. 950,400.00 

Volume Dry Gas Sampled - dscf 84.585 

Volume Dry Gas Sampled - dscm 2.395 

Stack Temperature- Deg. F 166.80 

Percent Moisture - % 1.37 

Velocity in the Stack - FPS 1.25 

Volumetric Flow Rate - ACFM 493,680 

Volumetric Flow Rate - DSCFM 397,005 

Isokinetic Sampling Rate - % 95.5 

15 

2 

3/18/13 

1255 - 1505 

0.40 

20.40 

28.91 

950,400.00 

84.44 

2.391 

166.80 

1.88 

1.20 

494,340 

394,798 

95.9 

3 

3/18/13 

1545 - 1800 

0.40 

20.50 

28.76 

950,400.00 

86.56 

2.451 

179.90 

1.15 

1.30 

500,280 

392,228 

98.9 
Run Number 

Naphthalene 

2-Methylnaphthalene 

Acenaphthylene 

Acenaphthene 

Fluorene 

Phenanthrene 

SUMMARY OF RESULTS 

Table Sa 

PAH Sampling Data 

Baghouse #2 

1 2 

ng 27400 48800 

ng/dscrn 11440.50 20409.87 

lbslhr 0.0170 0.0302 

lbs/ton 0.0020 0.0036 

ng 21700 42900 

ng/dscrn 9060.54 17942.28 

lbs/hr 0.0135 0.0265 

lbs/ton 0.0016 0.0032 

ng 2600 3060 

ng/dscrn 1085.59 1279.80 

lbslhr 0.0016 0.0019 

lbs/ton 0.0002 0.0002 

ng 1730 2230 

ng/dscrn 722.34 932.66 

lbs/hr 0.0011 0.0014 

lbs/ton 0.0001 0.0002 

ng 2230 3290 

ng/dscrn 931.11 1375.99 

lbslhr 0.0014 0.0020 

lbs/ton 0.0002 0.0002 

ng 13400 25100 

ng/dscrn 5594.99 10497.70 

lbslhr 0.0083 0.0155 

lbs/ton 0.0010 0.0019 

Production Rate (tonslhr) = 8.38 

3 Average 

43800 40000 

17870.26 16573.54 

0.0263 0.0245 

0.0031 0.0029 

29700 31433 

12117.50 13040.11 

0.0178 0.0193 

0.0021 0.0023 

4570 3410 

1864.55 1409.98 

0.0027 0.0021 

0.0003 0.0002 

2520 2160 

1028.15 894.38 

0.0015 0.0013 

0.0002 0.0002 

3480 3000 

1419.83 1242.31 

0.0021 0.0018 

0.0002 0.0002 

22400 20300 

9139.13 8410.61 

0.0134 0.0124 

0.0016 0.0015 
Run Number 

Anthracene 

Fluoranthene 

Pyrene 

Benzo( a )anthracene 

Chrysene 

Benzo(b )fluoranthene 

SUMMARY OF RESULTS 

Table 5b 

PAH Sampling Data 

Baghouse #2 

1 2 

ng 1040 1180 

ng/dscm 434.24 493.52 

lbs/hr 0.0006 0.0007 

lbs/ton 0.0001 0.0001 

ng 11100 73500 

ng/dscm 4634.66 30740.28 

lbs/hr 0.0069 0.0455 

lbs/ton 0.0008 0.0054 

ng 5200 42700 

ng/dscm 2171.19 17858.64 

lbs/hr 0.0032 0.0264 

lbs/ton 0.0004 0.0032 

ng 618 3260 

ng/dscm 258.04 1363.45 

lbs/hr 0.0004 0.0020 

lbs/ton 0.0000 0.0002 

ng 3660 29000 

ng/dscm 1528.18 12128.82 

lbs/hr 0.0023 0.0179 

lbs/ton 0.0003 0.0021 

ng 503 3320 

ng/dscm 210.02 1388.54 

lbs/hr 0.0003 0.0021 

lbs/ton 0.0000 0.0002 

Production Rate (tons/hr) = 8.38 

3 Average 

1630 1283 

665.03 530.93 

0.0010 0.0008 

0.0001 0.0001 

15100 33233 

6160.75 13845.23 

0.0091 0.0205 

0.0011 0.0024 

7790 18563 

3178.29 7736.04 

0.0047 0.0114 

0.0006 0.0014 

672 1517 

274.17 631.89 

0.0004 0.0009 

0.0000 0.0001 

3830 12163 

1562.63 5073.21 

0.0023 0.0075 

0.0003 0.0009 

902 1575 

368.01 655.52 

0.0005 0.0010 

0.0001 0.0001 
Run Number 

Benzo(k)fluoranthene 

Benzo( e )pyrene 

Benzo( a )pyrene 

Perylene 

Indeno( 1 ,2,3-cd)pyrene 

Dibenz( a,h)anthracene 

SUMMARY OF RESULTS 

Table 5c 

PAH Sampling Data 

Baghouse #2 

1 2 

ng 172 1310 

ng/dscm 71.82 547.89 

lbslhr 1.07E-04 8.10E-04 

lbs/ton 1.27E-05 9.67E-05 

ng 364 1950 

ng/dscm 151.98 815.56 

lbs/hr 0.0002 0.0012 

lbs/ton 2.70E-05 1.44E-04 

ng 37 60 

ng/dscm 15.45 25.09 

lbslhr 2.30E-05 3.71E-05 

lbs/ton 2.74E-06 4.43E-06 

ng 33 55 

ng/dscm 13.78 23.00 

lbslhr 2.05E-05 3.40E-05 

lbs/ton 2.45E-06 4.06E-06 

ng 27.7 71.3 

ng/dscm 11.57 29.82 

lbslhr 1.72E-05 4.41E-05 

lbs/ton 2.05E-06 5.26E-06 

ng 4.7 9.6 

ng/dscm 1.96 4.02 

lbslhr 2.92E-06 5.94E-06 

lbs/ton 3.48E-07 7.09E-07 

Production Rate (tons/hr) = 8.38 

3 Average 

246 576.0 

100.37 240.02 

1.47E-04 3.55E-04 

1.76E-05 4.23E-05 

519 944 

211.75 393.10 

0.0003 0.0006 

3.71E-05 6.93E-05 

21 39 

8.57 16.37 

1.26E-05 2.42E-05 

1.50E-06 2.89E-06 

15 34.3 

6.12 14.30 

8.99E-06 2.12E-05 

1.07E-06 2.53E-06 

52.4 50 

21.38 20.92 

3.14E-05 3.09E-05 

3.75E-06 3.69E-06 

9.6 8 

3.92 3.30 

5.76E-06 4.87E-06 

6.87E-07 5.81E-07 
Run Number 

Benzo(g,h,i)perylene 

SUMMARY OF RESULTS 

Table 5d 

P AH Sampling Data 

Baghouse #2 

1 2 

ng 36.4 81.5 

ng/dscm 15.20 34.09 

lbslhr 2.26E-05 5.04E-05 

lbs/ton 2.70E-06 6.02E-06 

Production Rate (tonslhr) = 8.38 

19 

3 Average 

64.5 60.8 

26.32 25.20 

3.87E-05 3.72E-05 

4.61E-06 4.44E-06 
DISCUSSION OF RESULTS 

Three tests for particulate matter, hydrogen chloride, arsenic, cadmium, chromium, lead, 

manganese, nickel, mercury, dioxins/:furans, polychlorinated biphenyls, and polycyclic aromatic 

hydrocarbons were performed on the Furnace #2 Baghouse. The results of the tests appear to be an 

accurate and valid representation of the actual emissions of the stack. Leak checks were performed 

on the sampling systems to maintain the integrity of the samples and no leaks were detected. 

Hydrogen Chloride 

The moisture percentages were consistent with the largest variation being 66.1 percent from the 

mean value of 0.84 percent. The flow rates were consistent with the largest variation being 0.61 

percent from the mean value of 444,697 DSCFM. The isokinetic sampling rates were within the 

specified limits (90 to 110 % isokinetic) with the largest variation being 4.9 percent from 100 

percent. 

Particulate/Metals 

The moisture percentages were consistent with the largest variation being 22.37 percent from the 

mean value of 0.51 percent. The flow rates were consistent with the largest variation being 0.53 

percent from the mean value of 448,236 DSCFM. The isokinetic sampling rates were within the 

specified limits (90 to 110 % isokinetic) with the largest variation being 6. 7 percent from 100 

percent. 

Mercury 

Paired samples for mercury were taken simultaneously for each run. The relative deviation 

percentages were within the allowable limits of the method for each run. 

20 
Dioxins!Furans/PCBs 

The moisture percentages were consistent with the largest variation being 9.42 percent from the 

mean value of 0.81 percent. The flow rates were consistent with the largest variation being 0.93 

percent from the mean value of 442,555 DSCFM. The isokinetic sampling rates were within the 

specified limits (90 to 110 % isokinetic) with the largest variation being 6.8 percent from 100 

percent. 

Polycyclic Aromatic Hydrocarbons (P AH) 

The moisture percentages were consistent with the largest variation being 28.18 percent from the 

mean value of 1.47 percent. The flow rates were consistent with the largest variation being 0.62 

percent from the mean value of 394,677 DSCFM. The isokinetic sampling rates were within the 

specified limits (90 to 110 % isokinetic) with the largest variation being 4.5 percent from 100 

percent. 

21 
SAMPLING AND ANALYTICAL PROCEDURES 

The testing followed the procedures in the Appendix to the Code of Federal Regulations, Title 

40, Chapter 1, Part 60, Methods 1, 2, 3A, 4, 5d, 26A, 29, and 30B; and California Air Resources 

Board Methods 428 (CARB 428), and 429 (CARB 429). Three tests were performed for each 

pollutant. The manometer was zeroed and leak checks were performed before each test. Leak 

checks were performed on the sampling systems to maintain the integrity of the samples and no 

leaks were detected. 

A velocity traverse was performed on the inlet to the baghouse prior to the testing according to EPA 

Method 5D. The inlet velocity was used to calculate the isokinetic setup and determine the velocity 

in the outlet of the baghouse for each test. Once the preliminary inlet velocity was determined, 

Equation 5D-3 from Method 5D was used to determine the dilution air flow rate of the baghouse 

and applied to the baghouse velocity. 

Hydrogen Chloride 

The hydrogen chloride samples were taken according to EPA Methods 5D and 26A. For each run, 

samples of five minute duration were taken isokinetically from each of the twenty-four traverse 

points for a total sampling time of 120 minutes. Blank samples were collected for each reagent 

used during sampling and analyzed for contamination. 

The "front-half'' of the sampling train consisted of a glass nozzle, heated glass probe (248op + 

25°F), and heated Teflon filter support with a quartz fiber filter (248op + 25op). The "back-half'' of 

the sampling train contained the following impingers: 

lm:Qinger Contents 

1 0.1 N. H2S04 

2 0.1 N. H2S04 

3 Empty 

4 Silica Gel 

Amount 

100ml 

100ml 

400g 

22 

Parameter 

HCI 

HCl 

Moisture 

Moisture 
The impingers were measured to determine moisture content and then rinsed and recovered using 

de-ionized water into a leak-free amber glass sample jar with a Teflon lid. 

The samples were analyzed using ion chromatography by Maxxam Analytics, Inc located in 

Mississauga, Ontario. 

Particulate Matter/Multiple Metals 

The particulate matter and multiple metals samples were taken according to EPA Methods 5D and 

29. For each run, samples often minute duration were taken isokinetically from each of the twentyfour traverse points for a total sampling time of 240 minutes. Data was recorded in five minute 

intervals. Blank samples were collected for each reagent used during sampling and analyzed for 

contamination. 

The "front-half' of the sampling train consisted of a glass nozzle, heated glass probe (248°F + 

25°F), and heated Teflon filter support with a quartz fiber filter (248°F + 25°F). The "back-half' of 

the sampling train contained the following impingers: 

Impinger 

1 

2 

3 

4 

Contents 

5%HN03/l O%H202 

5%HN03/l O%H202 

Empty 

Silica Gel 

Amount 

lOOml 

lOOml 

400 g 

Parameter 

Metals 

Metals 

Metals 

Moisture 

The filter was recovered and collected in a sealed petri dish. The "front-half' of the sampling 

train (nozzle, probe, and front-half filter holder) was rinsed with acetone and collected in a leak-free 

amber glass sampling bottle with teflon lid. The "front-half' of the sampling train (nozzle, probe, 

and front-half of filter holder) was then rinsed three times with a total of 1 OOml of 0.1 N HN03 

and collected in a leak-free amber glass sample bottle with Teflon lid. The impinger contents 

were measured to determine the moisture content and then collected in a leak-free amber glass 

sample bottle with teflon lid. The back-half of the filter holder, impingers, and connecting 

23 
glassware were then rinsed with three times with a total of 1 OOml of 0.1 N HN03 and collected 

into the same sample bottle as the impinger contents. 

The metals samples were analyzed by ICP-MS and ICP-AES according to EPA Method 29, by 

Maxxam Analytics, Inc located in Mississauga, Ontario. The particulate samples were analyzed 

using gravimetric analysis by TEST, Incorporated located in Poca, West Virginia. 

Mercury 

The mercury samples were taken according to EPA Methods 30B. Samples of eighteen minute 

duration were taken from each of the seven traverse points for a total sampling time of 126 

minutes on each stack. Each run consisted of paired samples. Blank and spiked samples were 

taken, recovered, and analyzed for contamination. The sampling train consisted of a two stage 

sorbent trap, heated probe, sample line, and gas meter and pump. The paired sorbent traps were 

contained within the heated probe. 

The samples were analyzed for mercury by Ohio Lumex, Twinsburg, Ohio. 

Dioxins/Furans/Polychlorinated Biphenyls 

The dioxins/furans/PCBs samples were taken according to EPA Method 5D and CARB 428. For 

each run, samples of five minute duration were taken isokinetically from each of the twenty-four 

traverse points for a total sampling time of 120 minutes. Data was recorded in five minute 

intervals. Blank samples were collected for each reagent used during sampling and analyzed for 

contamination. A train blank was also performed and analyzed for contamination. 

The "front-half' of the sampling train consisted of a glass nozzle, heated glass probe (248op ± 

25op), and heated Teflon filter support with a quartz fiber filter (248op ± 25op). The "back-half' of 

the sampling train contained the following impingers: 

24 
lmQinger Contents Amount Parameter 

Water-cooled condenser coil 

Water-cooled XAD-2 adsorbent tube 

1 Empty --------- Dioxins/Furans/PCBs 

2 De-ionized water 100m1 Dioxins/Furans/PCBs 

3 empty Dioxins/Furans/PCBs 

4 Silica Gel 400g Moisture 

The filter was recovered and collected in a sealed petri dish. The "front-half' of the sampling 

train (nozzle, probe, and front-half of filter holder) was rinsed and brushed three times with 

methanol, benzene, and methylene chloride and collected in a leak-free amber glass sampling 

bottle with teflon lid. The impinger contents were measured to determine the moisture content 

and then collected in a leak-free amber glass sample bottle with teflon lid. The "back-half' of 

the filter holder, connecting glassware before the condenser, and the condenser was rinsed with 

methanol, benzene, and methylene chloride and collected in a leak-free amber glass sampling 

bottle with teflon lid. The XAD-2 trap was recovered, covered with aluminum foil and 

refrigerated. 

The dioxins/furans/PCBs samples were analyzed by high resolution mass spectrometry according 

to CARB 428, by Maxxam Analytics, Inc located in Mississauga, Ontario. 

Polycyclic Aromatic Hydrocarbons 

The polycyclic aromatic hydrocarbon samples were taken according to CARB 429. For each run, 

samples of five minute duration were taken isokinetically from each of the twenty-four traverse 

points for a total sampling time of 120 minutes. Data was recorded in five minute intervals. Blank 

samples were collected for each reagent used during sampling and analyzed for contamination. 

The "front-half' of the sampling train consisted of a glass nozzle, heated glass probe (248<>p ± 

25<>p), and heated Teflon filter support with a quartz fiber filter (248<>p ± 25°F). The "back-half' of 

the sampling train contained the following impingers: 

25 
Im,ninger Contents Amount Parameter 

Water-cooled condenser coil 

Water-cooled XAD-2 adsorbent tube 

1 Empty --------- PAH 

2 3mM NaHC03/2.4mM Na2C03 lOOml PAH 

3 3mM NaHC03/2.4mM Na2C03 lOOml PAH 

4 empty PAH 

5 Silica Gel 400 g Moisture 

The filter was recovered and collected in a sealed petri dish. The impinger contents were 

measured to determine the moisture content and then collected in a leak-free amber glass sample 

bottle with Teflon lid. The "front-half' and "back-half' of the sampling train (nozzle, probe, and 

front and back-half of filter holder, connecting glassware, and condenser) were rinsed three times 

each with acetone, hexane, and methylene chloride and collected in a leak-free amber glass 

sample bottle with Teflon lid. The impingers and connecting glassware were then rinsed three 

times each with acetone, hexane, and methylene chloride and collected into the same sample 

bottle as the impinger contents. The XAD-2 trap was recovered, covered with aluminum foil and 

refrigerated. 

The P AH samples were analyzed according to CARB 429 by Maxxam Analytics, Inc located in 

Mississauga, Ontario. 

26 
Baghouse 2 

N 

-...] 

Baghouse 2 

40' 

Duct Dimensions = 40' x 165' 

Area OfDuct = 950,400.0 sq. inches 

Drawings Not to Scale 

165' 

• • • • 

• • • • 

• • • • 

• • • • - ~ .... ""'1 

• • • • - - ~- -~ .. - ~ -~ .~ - "" .. 

• • • • 

• • • • 

• • • • 

• • • • ------- --~---- ------L ··---- --~--- --

• 

• 

Traverse 

Points 

1 

2 

3 

4 

• 

• 

• • I 

----------~- ---·· I 

• 

Feet from 

Stack Wall 

5 

15 

25 

35 

• 
Furnace #2 Baghouse Inlet 

Gas Flow ---

5 I .N 

696" 144" 

Traverse Percent of Inches From 

Points Diameter Stack Wall 

1 2.1 3 3/16 

2 6.7 10 2/16 

3 11.8 1714/16 

4 17.7 26 13/16 

5 25.0 37 14116 

Inside Diameter of Stack = 12 ft. 7.5 m. 6 35.5 53 13/16 

Port to Upstream Distance = 12 ft. 0.0 m. 7 64.5 97 11116 

Port to Downstream Distance = 58 ft. 0.0 in. 8 75.0 113 10/16 

Area Of Stack = 18,026.7 sq. inches 9 82.3 124 11116 

Port to Upstream Distance = 0.95 Stack Diameters 10 88.2 133 10/16 

Port to Downstream Distance = 4.59 Stack Diameters 11 93.3 141 6/16 

Drawings Not to Scale 12 97.9 148 5/16 
APPENDIXES 

A - Computer Data and Example Calculations 

B - Pre-flow Data 

C - Analytical Data 

D - Field Data Sheets 

E - Calibration Data 

F - Chain of Custody 

G - Plant Operational Data 

29 
APPENDIX A 

COMPUTER DATA 

AND 

EXAMPLE CALCULATIONS 

.::.• 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #2 

PROJECT#: TI1550 

Run Number 1 2 3 

Date 3/19/13 3/19/13 3/19/13 

Time 855 - 1110 1215 - 1425 1600 - 1815 

0 = Sample time 120 120 120 minutes 

Pb = Barometric Pressure at Port Elevation 29.05 29.05 29.05 in. Hg 

Vm =Vol. of Metered Gas- meter cond., cal corr. 108.701 107.025 101.416 cu. ft. 

Tm =Meter Temperature 80.8 80.4 53.0 Farenheit 

Tm =Meter Temperature 540.8 540.4 513.0 Rankine 

Po = Meter Orifice Pressure 2.30 2.30 2.00 in. H20 

Pma =Meter Pressure Absolute 29.22 29.22 29.20 in. Hg 

Vtwet =Sampled Gas Volume Wet 125.080 121.557 123.337 cu. ft. 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 103.659 102.137 101.876 cu.ft 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 2.935 2.892 2.885 cu. Meter 

C02 =% C02, dry 0.40 0.40 0.50 % 

02 =% 02, dry 20.40 20.50 20.40 % 

co =%co, dry 0.00 0.00 0.00 % 

N2 = %N2,dry (N2+CO) = 1 OO-(C02+02) 79.20 79.10 79.10 % 

EA =Excess Air 3,469.4 4,442.0 3,633.1 % 

Vw =Volume Water 31.0 10.8 13.5 grams 

H20 =mgas 1.39 0.50 0.62 % 

H20 = Moisture in Gas at Saturation 26.07 24.14 30.78 % 

Md = Dry Molecular Weight of Stack Gas 28.88 28.88 28.90 

Mw =Wet Molecular Weight of Stack Gas 28.73 28.83 28.83 

Psg = Stack Pressure, gauge - measured 0.10 0.00 0.10 in. H20 

Psa = Stack Pressure, absolute 29.06 29.05 29.06 in. Hg 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #2 

PROJECT#: TI1550 

Run Number 1 2 3 

Ts =Stack Temperature 150.30 147.20 157.10 Farenheit 

Ts = Stack Temperature 338.72 337.00 342.50 Kelvin 

Ts =Stack Temperature 610.3 607.2 617.1 Rankine 

\I L1 P = A vg. Sum. of Pressure Square Root 0.022 0.022 0.022 

Vs = Velocity in the Stack 81.0 80.7 81.4 ft/min 

Vs = Velocity in the Stack 1.35 1.30 1.40 ft/sec 

As = Effective Stack Area 950,400.0 950,400.0 950,400.0 sq. m. 

Qa =Volumetric Flow Rate at stack cond. 534,600 532,620 537,240 acfm 

Qs = Volumetric Flow Rate, stand. cond., dry 442,970 447,432 443,690 dscfm 

IR = I so kinetic Ratio (V n/V s )* 100 104.9 102.3 102.9 % 
TEST, Inc. romments: 

HCI Sampling Data 

Project# TI1550 Meter Box # 2010 %C02 0.40 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0203 %02 20.40 1 705.2 693.2 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 710.3 722.7 

Operator br Nozzle# %N2 79.20 3 599.1 606.9 

Run# 1 Nozzle Dia. (in.) 1.5 Assumed Moist % 2.00 4 872.3 895.1 

Date 3/19/13 Stack Dia.(in.) Final Moist. % 1.39 5 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic % 104.9 6 

Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0.001 cfm@ 10 "Hg 

Filter# Leak Check Vol. Final Leak Rate 0.001 cfm@ 10 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 855 898.665 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

11-6 900 903.210 0.0005 2.30 0.864 5.0 138 246 252 68 77 76 

5 905 907.007 0.0005 2.30 0.864 5.0 138 247 251 65 80 78 

4 910 911.502 0.0005 2.30 0.864 5.0 143 252 251 67 82 80 

3 915 918.908 0.0005 2.30 0.864 5.0 142 252 249 66 85 82 

2 920 920.502 0.0005 2.30 0.864 5.0 146 249 251 66 89 87 

1 925 924.975 0.0005 2.30 0.864 5.0 155 251 251 63 82 80 

10-6 935 929.403 0.0005 2.30 0.864 5.0 143 241 250 58 87 86 

5 940 933.807 0.0005 2.30 0.864 5.0 143 247 250 60 82 80 

4 945 938.305 0.0005 2.30 0.864 5.0 147 253 250 63 85 84 

3 950 942.801 0.0005 2.30 0.864 5.0 146 250 250 68 82 80 

2 955 947.206 0.0005 2.30 0.864 5.0 145 249 250 47 78 77 

1 1000 951.406 0.0005 2.30 0.864 5.0 147 248 249 50 78 76 

9-6 1010 955.808 0.0005 2.30 0.864 5.0 175 244 250 51 83 80 

5 1015 960.305 0.0005 2.30 0.864 5.0 176 248 250 51 81 79 

4 1020 964.803 0.0005 2.30 0.864 5.0 178 253 250 53 80 78 

3 1025 969.206 0.0005 2.30 0.864 5.0 165 252 249 53 82 80 

2 1030 974.002 0.0005 2.30 0.864 5.0 151 249 250 53 81 78 

1 1035 978.203 0.0005 2.30 0.864 5.0 152 250 250 54 82 81 

8-6 1045 982.706 0.0005 2.30 0.864 5.0 146 249 251 52 77 75 

5 1050 987.003 0.0005 2.30 0.864 5.0 146 249 249 56 80 78 

4 1055 991.702 0.0005 2.30 0.864 5.0 149 249 249 56 80 79 

3 1100 996.103 0.0005 2.30 0.864 5.0 149 252 249 57 83 82 

2 1105 1,000.702 0.0005 2.30 0.864 5.0 143 248 251 57 80 80 

1 1110 1,005.203 0.0005 2.30 0.864 5.0 145 250 250 58 84 82 
Example Calculations 

Run Number 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 

Vw 31 Water weight gain Ds 0 

Pm 2.3 "H20 Meter pressure As 950,400.0 

Avg L1 P 0.001 "H20 Differential pressure Dn 1.5 

AvgSqrti1 P 0.022 "H20 Sqrt Diff. press. Tt 120 

%C02 0.40 Carbon Dioxide %CO 0.00 

%02 20.40 Oxygen 

Vm 106.538 acf 

Ps 0.10 "H20 

Tm 80.8 (F) 

Ts 150.3 (F) 

Vmstd = 17.65 * Vm * [ Pb + ~J Tm(R) 

Vwgas = 0.0471 * Vw = 0.0471 * 

%N2 79.20 

108.701 (acf * Y) Dry Gas Volume 

29.06 "Hg Stack Pressure 

540.8 (R) Meter Temperature 

610.3 (R) Stack Temperature 

~ 17.65 * 108.701 ' [ 

2.30 

29.05 + 13.6 

540.8 l 

31 1.4601 sft 3 

Pitot Cal 

m. Stack Diameter 

Sq in. Stack Area 

m Nozzle Diameter 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

103.659 sft j 

1.728 scfm 

Bws= Vwgas Bws*100 = 1.39 %Moist. Md = 28.880 

Vmstd + Vwgas 

Ts (R) 

Vs = 5129.4 * Cp * \ Ps * Mw 

5129.4 * 0.84 

1-Bws = 0.9861 

* sqrt L1 P 

610.3 

29.06 * 28.729 * 0.022 

ACFM= Vs *As 

144 

81.0 * 950400.0 

144 

534,600 ACFM 

====== MW = 28.729 ===== 

81.0 fpm 1.35 fps ==== ====== 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

534,600 * 528 * 29.06 * 0.9861 

610.3 * 29.92 

442,970 DSCFM 

0

/o Iso. = 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (DnY'2 

1,039 * 103.659 

0.9861 * 29.06 * 120 

* 610.3 104.9 % 

* 81.0 * 2.25000 
TEST, Inc. I Comments: 

HCI Sampling Data 

Project# TI1550 Meter Box # 20 I 0 %C02 0.40 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0203 %02 20.50 1 710 688.9 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 710.1 721.1 

Operator br Nozzle# %N2 79.10 3 604.5 609.3 

Run# 2 Nozzle Dia. (in.) 1.5 Assumed Moist % 2.00 4 895.1 911.2 

Date 3/19/13 Stack Dia.(in.) Final Moist. % 0.50 5 

Sample Time 120 Static Press.("H20) Final Isokinetic % 102.3 6 

Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0.001 cfm@ 15 "Hg 

Filter# Leak Check Vol. Final Leak Rate 0.001 cfm@ 10 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 1215 9.705 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

7-8 1220 10.208 0.0005 2.30 0.864 5.0 152 242 246 58 78 76 

7 1225 15.718 0.0005 2.30 0.864 5.0 150 249 249 63 76 74 

6 1230 19.307 0.0005 2.30 0.864 5.0 149 253 251 66 80 78 

5 1235 23.809 0.0005 2.30 0.864 5.0 151 250 254 67 86 84 

4 1240 28.400 0.0005 2.30 0.864 5.0 158 251 252 59 82 80 

3 1245 32.908 0.0005 2.30 0.864 5.0 162 251 250 61 83 81 

2 1250 37.507 0.0005 2.30 0.864 5.0 157 251 249 60 84 82 

I 1255 42.105 0.0005 2.30 0.864 5.0 154 250 248 64 80 78 

6-8 1305 46.902 0.0005 2.30 0.864 5.0 120 246 248 53 78 76 

7 1310 51.203 0.0005 2.30 0.864 5.0 126 251 248 61 77 75 

6 1315 55.801 0.0005 2.30 0.864 5.0 128 252 251 61 78 77 

5 1320 59.107 0.0005 2.30 0.864 5.0 131 251 252 55 74 72 

4 1325 65.506 0.0005 2.30 0.864 5.0 136 252 251 61 78 76 

3 1330 69.405 0.0005 2.30 0.864 5.0 136 251 251 65 79 77 

2 1335 73.902 0.0005 2.30 0.864 5.0 131 249 249 48 79 78 

I 1340 78.505 0.0005 2.30 0.864 5.0 142 251 249 52 83 80 

5-8 1350 83.104 0.0005 2.30 0.864 5.0 146 249 249 49 88 86 

7 1355 87.502 0.0005 2.30 0.864 5.0 162 249 249 51 89 88 

6 1400 91.908 0.0005 2.30 0.864 5.0 158 251 250 51 90 88 

5 1405 96.409 0.0005 2.30 0.864 5.0 155 252 250 50 85 82 

4 1410 101.003 0.0005 2.30 0.864 5.0 155 250 250 50 79 78 

3 1415 105.007 0.0005 2.30 0.864 5.0 156 250 251 53 78 77 

2 1420 110.008 0.0005 2.30 0.864 5.0 160 249 251 55 83 82 

I 1425 114.601 0.0005 2.30 0.864 5.0 158 247 250 56 85 83 
Example Calculations 

Run Number 2 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 10.8 Water weight gain Ds 0 in. Stack Diameter 

Pm 2.3 "H20 Meter pressure As 950,400.0 Sq in. Stack Area 

Avg!::. P 0.001 "H20 Differential pressure Dn 1.5 in Nozzle Diameter 

Avg Sqrt!::. P 0.022 "H20 Sqrt Diff. press. Tt 120 min Sample Time 

%C02 0.40 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.50 Oxygen 

Vm 104.896 acf 

Ps 0.00 "H20 

Tm 80.4 (F) 

Ts 147.2 (F) 

Vmstd = 17.65 * Vm * [ Pb + 1~] Tm(R) 

%N2 79.10 

107.025 (acf* Y) Dry Gas Volume 

29.05 "Hg Stack Pressure 

540.4 (R) Meter Temperature 

607.2 (R) Stack Temperature 

= 17.65 • 107.025 • [ 

2.30 

29.05 + 13.6 

540.4 } 

Nitrogen 

102.137 sft 5 

1.702 scfm 

Vwgas = 0.0471 * Vw = 0.0471 * 10.8 0.5087 sft 3 

Bws= Vwgas 

Vmstd + Vwgas 

Vs = 5129.4 * 

5129.4 * 

Ts (R) 

\Ps * Mw 

0.84 

Bws* I 00 = 0.50 % Moist. Md = 28.884 ===== 1-Bws = 0.9950 MW = 28.830 

* sqrt !::. P 

607.2 

29.05 * 28.830 * 0.022 = 80.7 fpm 1.3 ==== ===== 

ACFM= Vs *As 

144 

80.7 * 950400.0 

144 

532,620 ACFM 

fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

532,620 * 528 * 29.05 * 0.9950 

607.2 * 29.92 

447,432 DSCFM 

% Iso.= 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (Dn)"2 

1,039 * 102.137 * 607.2 

0.9950 * 29.05 * 120 * 80.7 * 2.25000 

102.3 % 
TEST, Inc. I Comments: 

HCI Sampling Data 

Project# TI1550 Meter Box # 20 I Omst %C02 0.50 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.40 I 709.9 756.3 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 710.5 659.6 

Operator br Nozzle# %N2 79.10 3 603.5 603.5 

Run# 3 Nozzle Dia. (in.) 1.5 Assumed Moist % 2.00 4 896.9 914.9 

Date 3/19/13 Stack Dia.(in.) Final Moist. % 0.62 5 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic % 102.9 6 

Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0 cfm@ 10 "Hg 

Filter# Leak Check Vol. Final Leak Rate 0 cfm@ 10 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 1600 730.157 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

4-6 1605 734.300 0.0005 2.00 0.814 3.0 155 255 249 61 51 49 

5 1610 738.420 0.0005 2.00 0.814 3.0 156 254 250 60 51 49 

4 1615 742.600 0.0005 2.00 0.814 3.0 154 247 251 60 54 52 

3 1620 746.790 0.0005 2.00 0.814 3.0 154 251 253 64 54 54 

2 1625 750.920 0.0005 2.00 0.814 3.0 153 254 252 61 54 52 

1 1630 755.075 0.0005 2.00 0.814 3.0 153 262 250 64 54 53 

3-6 1640 759.140 0.0005 2.00 0.814 3.0 155 266 254 61 53 49 

5 1645 763.300 0.0005 2.00 0.814 3.0 157 262 250 57 52 50 

4 1650 767.405 0.0005 2.00 0.814 3.0 156 256 250 58 54 51 

3 1655 771.515 0.0005 2.00 0.814 3.0 150 257 250 58 53 51 

2 1700 775.645 0.0005 2.00 0.814 3.0 154 260 249 60 54 52 

1 1705 779.725 0.0005 2.00 0.814 3.0 153 259 249 60 54 52 

2-6 1715 783.850 0.0005 2.00 0.814 3.0 155 268 248 67 56 52 

5 1720 787.975 0.0005 2.00 0.814 3.0 156 260 251 58 57 53 

4 1725 792.080 0.0005 2.00 0.814 3.0 159 254 250 56 56 53 

3 1730 796.245 0.0005 2.00 0.814 3.0 161 256 249 54 55 53 

2 1735 800.400 0.0005 2.00 0.814 3.0 156 259 249 55 55 53 

1 1740 804.560 0.0005 2.00 0.814 3.0 157 260 250 56 56 54 

1-6 1750 808.700 0.0005 2.00 0.814 3.0 160 267 250 64 54 52 

5 1755 812.845 0.0005 2.00 0.814 3.0 163 261 251 58 54 52 

4 1800 817.000 0.0005 2.00 0.814 3.0 164 258 252 56 54 53 

3 1805 821.225 0.0005 2.00 0.814 3.0 164 256 252 54 55 53 

2 1810 824.410 0.0005 2.00 0.814 3.0 162 258 251 52 54 53 

l 1815 828.600 0.0005 2.00 0.814 3.0 163 260 250 55 54 51 
Example Calculations 

Run Number 3 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 

Vw 13.5 Water weight gain Ds 0 

Pm 2 "H20 Meter pressure As 950,400.0 

Avg ~ P 0.001 "H20 Differential pressure Dn 1.5 

Avg Sqrt ~ P 0.022 "H20 Sqrt Diff. press. Tt 120 

%C02 0.50 Carbon Dioxide %CO 0.00 

%02 20.40 Oxygen 

Vm 98.443 acf 

Ps 0.10 "H20 

Tm 53.0 (F) 

Ts 157.1 (F) 

Vmstd = 17.65 * Vm * [ Pb + 1~] Tm(R) 

%N2 79.10 

101.416 (acf * Y) Dry Gas Volume 

29.06 "Hg Stack Pressure 

513 (R) Meter Temperature 

617.1 (R) Stack Temperature 

= 17.65 * 101.416 * [ 29.05 + ~~~~ ]= 

513.0 

Vwgas = 0.0471 * Vw = 0.0471 * 13.5 0.6359 sft 3 

Pitot Cal 

Ill. Stack Diameter 

Sq in. Stack Area 

Ill Nozzle Diameter 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

101.876 sft j 

1.698 scfm 

Bws= Vwgas Bws*100 = 0.62 %Moist. Md = 28.896 ===== V mstd + V wgas 1-Bws = 0.9938 MW = 28.828 

Ts (R) 

Vs= 5129.4 * Cp * \Ps * Mw * sqrt ~ P 

617.1 

5129.4 * 0.84 29.06 * 28.828 * 0.022 81.4 fipm 

ACFM= Vs *As 

144 

81.4 * 950400.0 

144 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

% Iso. = 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (DnY'2 

1,039 * 101.876 

0.9938 * 29.06 * 120 

* 

* 

==== 

537,240 ACFM 

537,240 * 528 * 29.06 * 0.9938 

617.1 * 29.92 

617.1 102.9 % 

81.4 * 2.25000 

===1=.4==fps 

443,690 DSCFM 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #2 

PROJECT#: TI1550 

Run Number 

Date 

Time 

0 = Sample time 

Pb = Barometric Pressure at Port Elevation 

Vm = Vol. of Metered Gas - meter cond., cal corr. 

Tm = Meter Temperature 

Tm = Meter Temperature 

Po = Meter Orifice Pressure 

Pma = Meter Pressure Absolute 

Vtwet =Sampled Gas Volume Wet 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 

C02 =% C02, dry 

02 =% 02, dry 

co =%CO, dry 

N2 = %N2,dry (N2+CO) = 1 OO-(C02+02) 

EA =Excess Air 

Vw =Volume Water 

H20 =mgas 

H20 =Moisture in Gas at Saturation 

Md = Dry Molecular Weight of Stack Gas 

Mw = Wet Molecular Weight of Stack Gas 

Psg = Stack Pressure, gauge - measured 

Psa = Stack Pressure, absolute 

1 

3/20/13 

900 - 1315 

240 

29.15 

216.202 

74.0 

534.0 

2.22 

29.31 

247.268 

209.472 

5.932 

0.40 

20.40 

0.00 

79.20 

3,469.4 

17.9 

0.40 

22.81 

28.88 

28.84 

0.10 

29.16 

2 3 

3/20113 3/20/13 

900- 1315 1440 - 1850 

240 240 

29.15 29.05 

204.513 224.790 

56.5 81.8 

516.5 541.8 

2.00 2.30 

29.30 29.22 

245.471 252.611 

204.748 213.968 

5.798 6.059 

0.40 0.40 

20.40 20.50 

0.00 0.00 

79.20 79.10 

3,469.4 4,442.0 

27.2 22.9 

0.62 0.50 

27.90 21.43 

28.88 28.88 

28.81 28.83 

0.10 0.10 

29.16 29.06 

minutes 

in. Hg 

cu. ft. 

Farenheit 

Rankine 

in. H20 

in. Hg 

cu. ft. 

cu.ft 

cu. Meter 

% 

% 

% 

% 

% 

grams 

% 

% 

in. H20 

in. Hg 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #2 

PROJECT#: TI1550 

Run Number 1 2 3 

Ts =Stack Temperature 145.10 153.20 142.50 Farenheit 

Ts =Stack Temperature 335.83 340.33 334.39 Kelvin 

Ts = Stack Temperature 605.1 613.2 602.5 Rankine 

'I L1 P = Avg. Sum. ofPressure Square Root 0.022 0.022 0.022 

Vs = Velocity in the Stack 80.4 81.0 80.4 ft/min 

Vs = Velocity in the Stack 1.34 1.40 1.30 ft!sec 

As = Effective Stack Area 950,400.0 950,400.0 950,400.0 sq.m. 

Qa = Volumetric Flow Rate at stack cond. 530,640 534,600 530,640 acfm 

Qs = Volumetric Flow Rate, stand. cond., dry 449,461 445,847 449,401 dscfm 

IR = Isokinetic Ratio (Vn/Vs)*100 104.4 102.9 106.7 % 

Mn = Particulate Matter Catch, grams 0.0051 0.0042 0.0048 grams 

= Particulate Matter Catch, milligrams 5100.00 4233.33 4800.00 ug 

Ca = Particulate Matter Cone. - Stack Cond. 0.0003 0.0003 0.0003 gr/acf 

Cs = Particulate Matter Cone. - Dry Std. Cond. 0.0004 0.0003 0.0003 gr/dscf 

= Particulate Matter Emissions * 859.74 730.14 792.21 ug/dscm 

ER = Particulate Matter Emissions 1.54 1.15 1.16 lbs/hr 
TEST, Inc. ~Comments: 

Particulate/Metals Sampling Data ~----------------------------------------~ Project# TI1550 Meter Box# 2010 %C02 0.40 Imp. Initial Final ------ Plant Felman Productions LLC Meter Cal. (Y) 1.0203 %02 20.40 1 727.1 686.4 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 758.4 776.6 ----- ------ Operator br Nozzle# %N2 79.20 3 608.8 613.4 

Run# I Nozzle Dia. (in.) 1.5 Assumed Moist% 1.17 4 917.7 953.5 ----- ------ Date 3/20/13 Stack Dia.(in.) Final Moist.% 0.40 5 ------ Sample Time 240 Static Press.("H20) 0.10 Final Isokinetic % 104.4 6 ------------- Min/pt 5 Bar. Press. ("Hg) 29.15 Initial Leak Rate 0.001 cfm@ 14 "Hg --- Filter# 1007 Leak Check Vol. Final Leak Rate 0.001 cfm@ 12 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 900 277.406 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

11-6 905 282.005 0.0005 2.20 0.848 5.0 130 245 250 60 66 64 

6 910 286.306 0.0005 2.20 0.848 5.0 130 251 248 66 69 67 

5 915 290.507 0.0005 2.20 0.848 5.0 131 250 254 67 76 74 

5 920 294.803 0.0005 2.20 0.848 5.0 139 252 251 67 81 80 

4 925 299.205 0.0005 2.20 0.848 5.0 133 246 250 68 72 70 

4 930 303.601 0.0005 2.20 0.848 5.0 152 243 249 66 70 68 

3 935 307.908 0.0005 2.20 0.848 5.0 152 253 251 68 79 77 

3 940 312.305 0.0005 2.20 0.848 5.0 149 250 250 55 78 76 

2 945 316.705 0.0005 2.20 0.848 5.0 148 250 252 51 65 63 

2 950 321.107 0.0005 2.20 0.848 5.0 153 251 250 53 64 63 

1 955 325.407 0.0005 2.20 0.848 5.0 139 246 249 50 68 65 

1 1000 329.805 0.0005 2.20 0.848 5.0 139 251 249 51 70 68 

10-6 1010 334.108 0.0005 2.20 0.848 5.0 139 242 249 51 67 66 

6 1015 338.401 0.0005 2.20 0.848 5.0 142 251 250 51 70 68 

5 1020 343.103 0.0005 2.20 0.848 5.0 143 251 250 54 69 68 

5 1025 347.106 0.0005 2.20 0.848 5.0 141 247 250 53 71 70 

4 1030 351.406 0.0005 2.20 0.848 5.0 140 250 251 53 67 65 

4 1035 356.609 0.0005 2.20 0.848 5.0 145 251 250 56 71 70 

3 1040 360.104 0.0005 2.20 0.848 5.0 140 249 250 58 72 70 

3 1045 364.408 0.0005 2.20 0.848 5.0 141 251 250 58 72 71 

2 1050 368.805 0.0005 2.20 0.848 5.0 138 247 249 56 73 70 

2 1055 373.201 0.0005 2.20 0.848 5.0 148 255 250 56 74 72 

1 1100 377.508 0.0005 2.20 0.848 5.0 152 251 251 56 75 73 

1 1105 381.909 0.0005 2.20 0.848 5.0 146 247 251 57 75 73 

9-6 1115 386.306 0.0005 2.20 0.848 5.0 153 244 250 56 75 73 

6 1120 390.703 0.0005 2.20 0.848 5.0 152 248 250 55 75 74 

5 1 125 395.503 0.0005 2.20 0.848 5.0 160 250 250 55 74 72 

5 1130 399.408 0.0005 2.20 0.848 5.0 148 249 250 53 76 74 

4 1135 404.508 0.0005 2.20 0.848 5.0 152 252 250 55 76 74 

4 1140 408.202 0.0005 2.20 0.848 5.0 148 249 251 55 73 71 

3 1145 412.509 0.0005 2.20 0.848 5.0 155 252 250 56 75 74 
Example Calculations 

Run Number 

Pb 29.15 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 17.9 Water weight gain Ds 0 in. Stack Diameter 

Pm 2.22 "H20 Meter pressure As 950,400.0 Sq in. Stack Area 

Avg 11 P 0.001 "H20 Differential pressure Dn 1.5 in Nozzle Diameter 

Avg Sqrt 11 P 0.022 "H20 Sqrt Diff. press. Tt 240 mm Sample Time 

%C02 0.40 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.40 Oxygen 

Vm 211.9 acf 

Ps 0.10 "H20 

Tm 74.0 (F) 

Ts 145.1 (F) 

Vmstd = 17.65 * Vm * [ Pb + 1~] Tm(R) 

216.202 

29.16 

534 

605.1 

:::::: 17.65 

%N2 79.20 Nitrogen 

(acf* Y) Dry Gas Volume 

"Hg Stack Pressure 

(R) Meter Temperature 

(R) Stack Temperature 

• 216.202 • [ 

2.22 

29.15 + 13.6 

534.0 

] = 209.472 sft j 

3.491 scfm 

Vwgas=0.0471*Vw= 0.0471 * 17.9 0.8431 sft 3 

Bws= Vwgas 

Vmstd + Vwgas 

Ts (R) 

Vs=5129.4*Cp* \Ps*Mw 

5129.4 * 0.84 

Bws*100 = 0.40 %Moist. Md = 28.880 ===== 1-Bws = 0.9960 MW = 28.836 ===== 

* sqrt 11 P 

605.1 

29.16 * 28.836 * 0.022 = 80.4 fpm 1.34 :tips ==== ===== 

ACFM= Vs *As 

144 

80.4 * 950400.0 

144 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

%Iso.= 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (Dn)"2 

1,039 * 209.472 

530,640 ACFM 

530,640 * 528 * 29.16 * 0.9960 

605.1 * 29.92 

* 605.1 104.4 % 

0.9960 * 29.16 * 240 * 80.4 * 2.25000 

449,461 DSCFM 
TEST, Inc. I Comments: 

Particulate/Metals Sampling Data 

Project# TI1550 Meter Box # 20 I Omst %C02 0.40 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.40 1 709.1 667.4 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 692.8 719.1 

Operator csm Nozzle# %N2 79.20 3 600.2 610.6 

Run# 2 Nozzle Dia. (in.) 1.5 Assumed Moist % 1.80 4 913.4 945.6 

Date 3/20113 Stack Dia.(in.) Final Moist. % 0.62 5 

Sample Time 240 Static Press.("H20) 0.10 Final Isokinetic % 102.9 6 

Min/pt 5 Bar. Press. ("Hg) 29.15 Initial Leak Rate 0 cfm@ 12 "Hg 

Filter # I 006 Leak Check Vol. Final Leak Rate 0 cfm@ 10 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter(CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 900 881.892 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

4-6 905 886.015 0.0005 2.00 0.814 4.0 151 256 244 66 49 47 

6 910 889.995 0.0005 2.00 0.814 4.0 155 258 247 66 48 45 

5 915 893.990 0.0005 2.00 0.814 4.0 156 261 251 65 55 50 

5 920 898.065 0.0005 2.00 0.814 4.0 159 263 250 64 55 51 

4 925 902.140 0.0005 2.00 0.814 4.0 156 264 249 65 55 50 

4 930 906.255 0.0005 2.00 0.814 4.0 154 259 250 62 58 48 

3 935 910.380 0.0005 2.00 0.814 4.0 153 257 250 62 57 48 

3 940 914.500 0.0005 2.00 0.814 4.0 151 263 251 60 57 49 

2 945 918.585 0.0005 2.00 0.814 4.0 152 255 2479 60 56 49 

2 950 922.707 0.0005 2.00 0.814 4.0 156 258 250 60 57 49 

1 955 926.815 0.0005 2.00 0.814 4.0 160 259 252 61 57 50 

1 1000 830.957 0.0005 2.00 0.814 4.0 161 262 250 61 57 50 

3-6 1010 935.080 0.0005 2.00 0.814 4.0 161 257 250 65 54 49 

6 1015 939.215 0.0005 2.00 0.814 4.0 160 256 250 63 547 49 

5 1020 943.400 0.0005 2.00 0.814 4.0 163 255 250 60 55 50 

5 1025 947.435 0.0005 2.00 0.814 4.0 156 261 251 59 56 50 

4 1030 951.550 0.0005 2.00 0.814 4.0 150 265 250 59 57 50 

4 1035 955.660 0.0005 2.00 0.814 4.0 151 258 251 58 57 50 

3 1040 959.770 0.0005 2.00 0.814 4.0 153 259 250 59 55 49 

3 1045 963.880 0.0005 2.00 0.814 4.0 155 259 250 60 56 50 

2 1050 968.090 0.0005 2.00 0.814 4.0 152 259 250 59 57 50 

2 1055 972.125 0.0005 2.00 0.814 4.0 154 261 250 61 58 51 

I 1100 976.250 0.0005 2.00 0.814 4.0 156 265 250 64 56 50 

I 1105 980.395 0.0005 2.00 0.814 4.0 156 258 248 65 56 51 

2-6 1115 984.580 0.0005 2.00 0.814 4.0 151 261 250 67 51 49 

6 1120 988.700 0.0005 2.00 0.814 4.0 153 260 251 63 53 49 

5 1125 992.830 0.0005 2.00 0.814 4.0 154 261 250 62 52 49 

5 1130 996.965 0.0005 2.00 0.814 4.0 156 260 249 63 53 49 

4 1135 1,001.105 0.0005 2.00 0.814 4.0 151 261 251 56 51 49 

4 1140 1,005.325 0.0005 2.00 0.814 4.0 150 260 251 55 52 49 

3 1145 1,009.500 0.0005 2.00 0.814 4.0 150 258 249 55 53 49 
Example Calculations 

Run Number 2 

Pb 29.15 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 27.2 Water weight gain Ds 0 in. Stack Diameter 

Pm 2 "H20 Meter pressure As 950,400.0 Sq in. Stack Area 

Avg!::. P 0.001 "H20 Differential pressure Dn 1.5 in Nozzle Diameter 

Avg Sqrt!::. P 0.022 "H20 Sqrt Diff. press. Tt 240 mm Sample Time 

%C02 0.40 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.40 Oxygen 

Vm 198.518 acf 

Ps 0.10 "H20 

Tm 56.5 (F) 

Ts 153.2 (F) 

Vmstd = 17.65 * Vm * [ Pb + :] 

Tm(R) 

204.513 (acf* Y) 

29.16 "Hg 

516.5 (R) 

613.2 (R) 

= 17.65 * 204.513 

%N2 79.20 

Dry Gas Volume 

Stack Pressure 

Meter Temperature 

Stack Temperature 

* [ 29.15 + ~~~~ ]= 

516.5 

Nitrogen 

204.748 sft j 

3.412 scfm 

Vwgas = 0.0471 * Vw = 0.0471 * 27.2 1.2811 sft 3 

Bws= Vwgas 

Vmstd + Vwgas 

Vs = 5129.4 * 

5129.4 * 

Ts (R) 

\Ps * Mw 

0.84 

Bws* 100 = 0.62 % Moist. Md = 28.880 ===== 1-Bws = 0.9938 MW = 28.813 

* sqrt !::. P 

613.2 

29.16 * 28.813 * 0.022 81.0 fpm 1.4 ==== ===== 

ACFM= Vs *As 

144 

81.0 * 950400.0 

144 

534,600 ACFM 

fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

534,600 * 528 * 29.16 * 0.9938 

613.2 * 29.92 

445,847 DSCFM 

% Iso. = 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (DnY'2 

1,039 * 204.748 * 613.2 

0.9938 * 29.16 * 240 * 81.0 * 2.25000 

102.9 % 
TEST, Inc. I Comments: 

Particulate/Metals Sampling Data 

Project# TI1550 Meter Box # 201 0 %C02 0.40 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0203 %02 20.50 1 714.2 640.5 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 718.1 675.2 

Operator csm Nozzle# %N2 79.10 3 595 698.1 

Run# 3 Nozzle Dia. (in.) 1.5 Assumed Moist % 2.00 4 881.1 917.5 

Date 3/20/13 Stack Dia.(in.) Final Moist. % 0.50 5 

Sample Time 240 Static Press.("H20) 0.10 Final Isokinetic% 106.7 6 

Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0 cfm@ 15 "Hg 

Filter# 1005 Leak Check Vol. Final Leak Rate 0.001 cfm@ 15 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter(CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 1440 489.889 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

5-8 1445 494.400 0.0005 2.30 0.868 5.0 149 266 237 46 81 86 

8 1450 499.150 0.0005 2.30 0.868 5.0 150 256 239 42 80 86 

7 1455 503.705 0.0005 2.30 0.868 5.0 155 246 258 42 80 86 

7 1500 508.500 0.0005 2.30 0.868 5.0 152 250 261 41 81 86 

6 1505 513.125 0.0005 2.30 0.868 5.0 148 256 258 42 78 86 

6 1510 517.720 0.0005 2.30 0.868 5.0 147 252 251 42 76 84 

5 1515 522.215 0.0005 2.30 0.868 5.0 150 249 250 44 81 86 

5 1520 526.900 0.0005 2.30 0.868 5.0 151 249 251 43 81 85 

4 1525 531.500 0.0005 2.30 0.868 5.0 154 248 250 44 78 86 

4 1530 536.100 0.0005 2.30 0.868 5.0 157 250 249 46 80 86 

3 1535 540.650 0.0005 2.30 0.868 5.0 155 249 250 45 80 85 

3 1540 545.120 0.0005 2.30 0.868 5.0 155 251 252 46 74 83 

2 1545 549.805 0.0005 2.30 0.868 5.0 153 249 248 48 81 86 

2 1550 554.350 0.0005 2.30 0.868 5.0 150 250 250 51 83 87 

1 1555 558.900 0.0005 2.30 0.868 5.0 150 250 249 51 85 88 

I 1600 563.573 0.0005 2.30 0.868 5.0 148 251 250 52 85 88 

6-8 1610 567.865 0.0005 2.30 0.868 5.0 140 249 248 63 84 87 

8 1615 572.450 0.0005 2.30 0.868 5.0 140 249 249 60 82 87 

7 1620 577.000 0.0005 2.30 0.868 5.0 141 251 250 61 81 87 

7 1625 581.500 0.0005 2.30 0.868 5.0 139 249 250 65 81 87 

6 1630 586.285 0.0005 2.30 0.868 5.0 140 251 253 56 72 84 

6 1635 590.750 0.0005 2.30 0.868 5.0 139 250 252 55 70 83 

5 1640 595.395 0.0005 2.30 0.868 5.0 140 251 250 54 77 84 

5 1645 600.010 0.0005 2.30 0.868 5.0 141 250 248 55 75 83 

4 1650 604.400 0.0005 2.30 0.868 5.0 139 250 252 54 79 84 

4 1655 609.075 0.0005 2.30 0.868 5.0 142 251 249 55 80 85 

3 1700 613.670 0.0005 2.30 0.868 5.0 141 251 250 50 79 84 

3 1705 618.000 0.0005 2.30 0.868 5.0 141 251 251 55 80 86 

2 1710 622.850 0.0005 2.30 0.868 5.0 142 250 252 55 80 86 

2 1715 627.400 0.0005 2.30 0.868 5.0 140 251 249 59 79 85 

I 1720 632.035 0.0005 2.30 0.868 5.0 140 250 251 62 79 86 
Example Calculations 

Run Number 3 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 

Vw 22.9 Water weight gain Ds 0 

Pm 2.3 "H20 Meter pressure As 950,400.0 

Avg 1'1 P 0.001 "H20 Differential pressure Dn 1.5 

AvgSqrti'1 P 0.022 "H20 Sqrt Diff. press. Tt 240 

%C02 0.40 Carbon Dioxide %CO 0.00 

%02 20.50 Oxygen 

Vm 220.318 acf 

Ps 0.10 "H20 

Tm 81.8 (F) 

Ts 142.5 (F) 

Vmstd = 17.65 * Vm * [ Pb+ 1~] Tm(R) 

%N2 79.10 

224.79 (acf * Y) Dry Gas Volume 

29.06 "Hg Stack Pressure 

541.8 (R) Meter Temperature 

602.5 (R) Stack Temperature 

= 17.65 * 224.790 * [ 29.05 + ~:~ ]= 

541.8 

Vwgas = 0.0471 * Vw = 0.0471 * 22.9 1.0786 sft 3 

Pitot Cal 

m. Stack Diameter 

Sq in. Stack Area 

m Nozzle Diameter 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

213.968 sft 5 

3.566 scfm 

Bws= Vwgas Bws*100 = 0.50 %Moist. Md = 28.884 

Vmstd + Vwgas 

Ts (R) 

Vs= 5129.4*Cp* \Ps*Mw 

5129.4 * 0.84 

1-Bws = 0.9950 

* sqrt 1'1 P 

602.5 

29.06 * 28.830 * 0.022 

ACFM= Vs *As 

144 

80.4 * 950400.0 

144 

530,640 ACFM 

===== MW = 28.830 ===== 

fpm ==== 80.4 ===1=.3==fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

530,640 * 528 * 29.06 * 0.9950 449,401 DSCFM 

% Iso. = 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (Dn)'"'2 

1,039 * 213.968 

602.5 * 29.92 

* 602.5 

0.9950 * 29.06 * 240 * 80.4 * 2.25000 

106.7 % 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #2 

PROJECT#: TI1550 

Run Number 

Date 

Time 

0 = Sample time 

Pb = Barometric Pressure at Port Elevation 

Vm =Vol. of Metered Gas- meter cond., cal corr. 

Tm =Meter Temperature 

Tm =Meter Temperature 

Po = Meter Orifice Pressure 

Pma = Meter Pressure Absolute 

Vtwet =Sampled Gas Volume Wet 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 

C02 =% C02, dry 

02 =% 02, dry 

co =%co, dry 

N2 =%N2,dry (N2+CO) = 1 OO-(C02+02) 

EA =Excess Air 

Vw = Volume Water 

H20 =in gas 

H20 = Moisture in Gas at Saturation 

Md =Dry Molecular Weight of Stack Gas 

Mw =Wet Molecular Weight of Stack Gas 

Psg = Stack Pressure, gauge - measured 

Psa =Stack Pressure, absolute 

1 

3/19113 

855 - 1105 

120 

29.05 

102.044 

51.2 

511.2 

2.00 

29.20 

125.766 

102.868 

2.913 

0.40 

20.40 

0.00 

79.20 

3,469.4 

19.6 

0.89 

34.20 

28.88 

28.78 

0.10 

29.06 

2 3 

3/19/13 3/19/13 

1220- 1435 1555 - 1810 

120 120 

29.05 29.05 

99.957 110.187 

50.1 82.0 

510.1 542.0 

2.00 2.30 

29.20 29.22 

120.540 128.773 

100.981 104.844 

2.859 2.969 

0.40 0.50 

20.50 20.40 

0.00 0.00 

79.10 79.10 

4,442.0 3,633.1 

16.4 17.7 

0.76 0.79 

24.37 37.15 

28.88 28.90 

28.80 28.81 

0.10 0.10 

29.06 29.06 

minutes 

in. Hg 

cu. ft. 

Farenheit 

Rankine 

in. H20 

in. Hg 

cu. ft. 

cu.ft 

cu. Meter 

% 

% 

% 

% 

% 

grams 

% 

% 

in. H20 

in. Hg 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #2 

PROJECT#: TI1550 

Run Number 

Ts =Stack Temperature 

Ts =Stack Temperature 

Ts =Stack Temperature 

'I~ P = A vg. Sum. of Pressure Square Root 

Vs = Velocity in the Stack 

Vs = Velocity in the Stack 

As =Effective Stack Area 

Qa =Volumetric Flow Rate at stack cond. 

Qs = Volumetric Flow Rate, stand. cond., dry 

IR = Isokinetic Ratio (VnNs)*lOO 

1 

161.50 

344.94 

621.5 

0.022 

81.7 

1.36 

950,400.0 

539,220 

440,971 

104.6 

2 3 

147.60 165.00 

337.22 346.89 

607.6 625 

0.022 0.022 

80.8 81.9 

1.30 1.40 

950,400.0 950,400.0 

533,280 540,540 

446,676 440,019 

101.3 106.8 

Farenheit 

Kelvin 

Rankine 

ft/min 

ft/sec 

sq.m. 

acfm 

dscfm 

% 
TEST, Inc. ~Comments: 

Dioxin/Furans/PCB's Sampling Data ~----------------------------------------~ Project# TI1550 Meter Box# 2010 mst %C02 0.40 Imp. Initial Final ------ Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.40 1 344.5 353.7 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 713.5 700 ------ ------ Operator csm Nozzle# %N2 79.20 3 593.3 595 

Run# 1 Nozzle Dia. (in.) 1.5 Assumed Moist% 2.00 4 869.6 891.8 ------ ------ Date 3/19/13 Stack Dia.(in.) Final Moist.% 0.89 5 ------ Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic% 104.6 6 -------------- ------ Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0.005 cfm@ 11 "Hg --- Filter# ---- Leak Check Vol. Final Leak Rate 0.001 cfm@ 11 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 855 531.635 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

7-8 900 535.805 0.0005 2.00 0.814 5.0 151 262 232 51 52 50 

7 905 540.005 0.0005 2.00 0.814 5.0 157 260 249 47 54 51 

6 910 544.015 0.0005 2.00 0.814 5.0 159 263 249 45 54 52 

5 915 548.175 0.0005 2.00 0.814 5.0 160 262 252 47 59 52 

4 920 552.320 0.0005 2.00 0.814 5.0 166 259 250 52 60 52 

3 925 556.470 0.0005 2.00 0.814 5.0 166 264 251 53 55 52 

2 930 560.545 0.0005 2.00 0.814 5.0 164 261 251 55 55 52 

1 935 564.700 0.0005 2.00 0.814 5.0 161 260 251 52 52 50 

6-8 945 568.830 0.0005 2.00 0.814 5.0 160 253 250 60 52 49 

7 950 572.980 0.0005 2.00 0.814 5.0 163 260 251 57 53 50 

6 955 577.055 0.0005 2.00 0.814 5.0 163 258 249 52 52 50 

5 1000 581.190 0.0005 2.00 0.814 5.0 164 259 251 50 51 49 

4 1005 585.265 0.0005 2.00 0.814 5.0 169 258 251 51 50 48 

3 1010 589.400 0.0005 2.00 0.814 5.0 170 256 250 52 50 48 

2 1015 593.540 0.0005 2.00 0.814 5.0 161 257 250 56 51 49 

1 1020 597.695 0.0005 2.00 0.814 5.0 159 258 249 58 51 49 

5-8 1030 601.835 0.0005 2.00 0.814 5.0 161 266 249 58 50 48 

7 1035 605.800 0.0005 2.00 0.814 5.0 163 257 251 58 52 50 

6 1040 609.925 0.0005 2.00 0.814 5.0 165 257 250 56 51 48 

5 1045 614.050 0.0005 2.00 0.814 5.0 164 262 251 56 52 47 

4 1050 618.195 0.0005 2.00 0.814 5.0 163 259 250 57 52 49 

3 1055 622.350 0.0005 2.00 0.814 5.0 159 258 249 56 52 50 

2 ] 100 626.575 0.0005 2.00 0.814 5.0 158 257 250 56 52 50 

1 1105 630.688 0.0005 2.00 0.814 5.0 151 260 251 57 52 49 
Example Calculations 

Run Number 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 19.6 Water weight gain Ds 0 m. Stack Diameter 

Pm 2 "H20 Meter pressure As 950,400.0 Sq in. Stack Area 

Avg ~ P 0.001 "H20 Differential pressure Dn 1.5 in Nozzle Diameter 

Avg Sqrt ~ P 0.022 "H20 Sqrt Diff. press. Tt 120 mm Sample Time 

%C02 0.40 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.40 Oxygen %N2 79.20 Nitrogen 

Vm 99.053 acf 102.044 (acf * Y) Dry Gas Volume 

Ps 0.10 "H20 29.06 "Hg Stack Pressure 

Tm 51.2 (F) 511.2 (R) Meter Temperature 

Ts 161.5 (F) 621.5 (R) Stack Temperature 

Vmstd = 17.65 * Vm * ~ Pb + 1~] L Tm (R) 

~ 17.65 ' 102.044 ' [ 

2.00 

29.05 + 13.6 

511.2 

] = 102.868 sft j 

1.714 scfm 

Vwgas = 0.0471 * Vw = 0.0471 * 19.6 0.9232 sft 3 

Bws= Vwgas Bws*100 = 0.89 %Moist. 

Vmstd + Vwgas 

Ts (R) 

Vs= 5129.4 * Cp * \ Ps * Mw 

5129.4 * 0.84 

1-Bws = 0.9911 

* sqrt ~ P 

621.5 

29.06 * 28.783 * 0.022 

ACFM= Vs *As 

144 

81.7 * 950400.0 

144 

539,220 ACFM 

Md = 28.880 ===== MW = 28.783 ===== 

81.7 fpm 1.36 tips 

==== ===== 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

539,220 * 528 * 29.06 * 0.9911 440,971 DSCFM 

0/o Iso. = 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (DnY'2 

1,039 * 102.868 

0.9911 * 29.06 * 120 

621.5 * 29.92 

* 621.5 104.6 % 

* 81.7 * 2.25000 
TEST, Inc. I Comments: 

Dioxin!Furans/PCB's Sampling Data 

Project # TI1550 Meter Box# 2010 mst %C02 0.40 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.50 1 335.1 374.9 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 725.6 681.2 

Operator csm Nozzle# %N2 79.10 3 609.6 612.8 

Run# 2 Nozzle Dia. (in.) 1.5 Assumed Moist % 0.94 4 899 916.8 

Date 3119/13 Stack Dia.(in.) Final Moist.% 0.76 5 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic% 101.3 6 

Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0.001 cfm@ 12 "Hg 

Filter# ---- Leak Check Vol. Final Leak Rate 0.001 cfm@ 12 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter(CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 1220 632.460 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

4-6 1225 636.365 0.0005 2.00 0.814 5.0 139 263 233 67 49 48 

5 1230 640.300 0.0005 2.00 0.814 5.0 143 269 232 49 52 48 

4 1235 644.410 0.0005 2.00 0.814 5.0 149 258 239 49 52 49 

3 1240 648.530 0.0005 2.00 0.814 5.0 150 256 243 49 52 50 

2 1245 652.645 0.0005 2.00 0.814 5.0 151 264 249 45 52 49 

1 1250 656.830 0.0005 2.00 0.814 5.0 149 259 251 43 52 50 

3-6 1300 661.005 0.0005 2.00 0.814 5.0 145 263 249 47 52 49 

5 1305 665.160 0.0005 2.00 0.814 5.0 147 260 251 45 52 50 

4 1310 669.305 0.0005 2.00 0.814 5.0 144 258 250 48 52 50 

3 1315 673.510 0.0005 2.00 0.814 5.0 143 256 249 47 51 49 

2 1320 677.700 0.0005 2.00 0.814 5.0 150 259 251 49 51 49 

1 1325 681.845 0.0005 2.00 0.814 5.0 151 261 249 50 51 49 

2-6 1335 685.000 0.0005 2.00 0.814 5.0 153 259 253 47 50 49 

5 1340 689.135 0.0005 2.00 0.814 5.0 150 258 250 49 50 48 

4 1345 693.290 0.0005 2.00 0.814 5.0 150 259 250 50 51 48 

3 1350 697.415 0.0005 2.00 0.814 5.0 149 255 249 52 51 49 

2 1355 701.590 0.0005 2.00 0.814 5.0 140 260 250 52 51 49 

1 1400 709.710 0.0005 2.00 0.814 5.0 146 257 250 52 50 49 

1-6 1410 708.850 0.0005 2.00 0.814 6.0 153 261 249 64 51 49 

5 1415 712.970 0.0005 2.00 0.814 6.0 151 260 252 54 51 48 

4 1420 717.200 0.0005 2.00 0.814 6.0 151 259 249 52 51 48 

3 1425 721.305 0.0005 2.00 0.814 6.0 148 259 250 54 51 49 

2 1430 725.400 0.0005 2.00 0.814 6.0 144 261 251 56 52 50 

1 1435 729.487 0.0005 2.00 0.814 6.0 147 259 249 56 52 50 
Example Calculations 

Run Number 2 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 16.4 Water weight gain Ds 0 in. Stack Diameter 

Pm 2 "H20 Meter pressure As 950,400.0 Sq in. Stack Area 

Avg ~ P 0.001 "H20 Differential pressure Dn 1.5 m Nozzle Diameter 

Avg Sqrt ~ P 0.022 "H20 Sqrt Diff. press. Tt 120 min Sample Time 

%C02 0.40 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.50 Oxygen 

Vm 97.027 acf 

Ps 0.10 "H20 

Tm 50.1 (F) 

Ts 147.6 (F) 

Vmstd = 17.65 * Vm * [ Pb+ 1~] Tm(R) 

%N2 79.10 Nitrogen 

99.957 (acf* Y) Dry Gas Volume 

29.06 "Hg Stack Pressure 

510.1 (R) Meter Temperature 

607.6 (R) Stack Temperature 

~ 17.65 • 99.957 • [ 

2.00 

29.05 + 13.6 

510.1 

] = 100.981 sft _j 

1.683 scfm 

Vwgas = 0.0471 * Vw = 0.0471 * 16.4 0.7724 sft 3 

Bws= Vwgas 

Vmstd + Vwgas 

Vs = 5129.4 * 

5129.4 * 

Ts (R) 

\Ps * Mw 

0.84 

Bws*100 = 0.76 %Moist. Md = 28.884 ==== ===== 1-Bws = 0.9924 MW = 28.801 

* sqrt ~ P 

607.6 

29.06 * 28.801 * 0.022 1.3 ==8=0.=8=fpm ====== 

ACFM= Vs *As 

144 

80.8 * 950400.0 

144 

533,280 ACFM 

fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

533,280 * 528 * 29.06 * 0.9924 

607.6 * 29.92 

446,676 DSCFM 

% lso. = 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (Dn)"2 

1,039 * 100.981 * 607.6 

0.9924 * 29.06 * 120 * 80.8 * 2.25000 

101.3 % 
TEST, Inc. !Comments: 

Dioxin/Furans/PCB's Sampling Data ~--------------------------------------~ Project# TI1550 Meter Box# 2010 %C02 0.50 Imp. Initial Final --- Plant Felman Productions LLC Meter Cal. (Y) 1.0203 %02 20.40 1 340.9 339.8 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) _0_.8_4___ %CO __ _ 2 679.2 680.5 

Operator br Nozzle# %N2 79.10 3 609.6 609.6 ----- Run# 3 Nozzle Dia. (in.) 1.5 Assumed Moist% 2.00 4 891.8 909.3 ----- --- Date 3/19/13 Stack Dia.(in.) Final Moist.% 0.79 5 --- Sample Time 120 Static Press.("H20) _0_.1_0 ___ Final Isokinetic % 106.8 6 

Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0.001 cfm@ 10 "Hg 

Filter# Leak Check Vol. Final Leak Rate 0.001 cfm@ 10 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 1555 115.208 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

11-6 1600 119.607 0.0005 2.30 0.864 6.0 153 248 259 56 88 86 

5 1605 124.106 0.0005 2.30 0.864 6.0 151 247 252 52 84 82 

4 1610 128.703 0.0005 2.30 0.864 6.0 139 248 249 52 82 81 

3 1615 132.306 0.0005 2.30 0.864 6.0 153 249 252 56 81 80 

2 1620 137.806 0.0005 2.30 0.864 6.0 164 251 252 60 83 81 

1 1625 142.209 0.0005 2.30 0.864 6.0 154 251 250 59 83 80 

10-6 1635 146.707 0.0005 2.30 0.864 6.0 157 249 250 61 86 84 

5 1640 151.307 0.0005 2.30 0.864 6.0 160 249 249 60 85 83 

4 1645 155.804 0.0005 2.30 0.864 6.0 157 251 250 61 84 82 

3 1650 160.305 0.0005 2.30 0.864 6.0 156 250 251 61 84 82 

2 1655 164.808 0.0005 2.30 0.864 6.0 156 248 250 60 81 79 

1 1700 169.305 0.0005 2.30 0.864 6.0 166 251 251 63 83 82 

9-6 1710 173.803 0.0005 2.30 0.864 6.0 176 254 251 60 84 82 

5 1715 178.304 0.0005 2.30 0.864 6.0 175 249 250 57 83 81 

4 1720 182.805 0.0005 2.30 0.864 6.0 174 250 250 56 84 82 

3 1725 187.308 0.0005 2.30 0.864 6.0 171 250 249 55 80 81 

2 1730 191.806 0.0005 2.30 0.864 6.0 170 251 250 53 81 80 

1 1735 196.308 0.0005 2.30 0.864 6.0 169 250 251 52 80 79 

8-6 1745 200.708 0.0005 2.30 0.864 6.0 172 249 251 53 84 82 

5 1750 205.208 0.0005 2.30 0.864 6.0 178 251 250 53 83 81 

4 1755 209.707 0.0005 2.30 0.864 6.0 177 251 251 55 83 80 

3 1800 214.205 0.0005 2.30 0.864 6.0 174 249 250 56 80 78 

2 1805 218.705 0.0005 2.30 0.864 6.0 179 250 250 61 80 78 

1 1810 223.203 0.0005 2.30 0.864 6.0 178 250 250 65 83 82 
Example Calculations 

Run Number 3 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 17.7 Water weight gain Ds 0 in. Stack Diameter 

Pm 2.3 "H20 Meter pressure As 950,400.0 Sq in. Stack Area 

Avg !}. P 0.001 "H20 Differential pressure Dn 1.5 m Nozzle Diameter 

A vg Sqrt !}. P 0.022 "H20 Sqrt Diff. press. Tt 120 

%C02 0.50 Carbon Dioxide 

%02 20.40 Oxygen 

Vm 107.995 acf 

Ps 0.10 "H20 

Tm 82.0 (F) 

Ts 165.0 (F) 

Vmstd = 17.65 * Vm * [ Pb + 1~] Tm(R) 

110.187 

29.06 

542 

625 

::::: 17.65 

Vwgas = 0.0471 * Vw = 0.0471 * 17.7 

%CO 0.00 

%N2 79.10 

(acf* Y) Dry Gas Volume 

"Hg Stack Pressure 

(R) Meter Temperature 

(R) Stack Temperature 

* llO.l87 •[ 

2.30 

29.05 + 13.6 

542.0 

0.8337 sft 3 

min Sample Time 

Carbon Monoxide 

Nitrogen 

] = 104.844 sft j 

1.747 scfm 

Bws= Vwgas Bws*100 = 0.79 %Moist. Md = 28.896 

Vmstd + Vwgas 

Ts (R) 

Vs=5129.4*Cp* \Ps*Mw 

5129.4 * 0.84 

1-Bws = 0.9921 

* sqrt !}. P 

625 

29.06 * 28.810 * 

===== MW = 28.810 

0.022 ===8=1.=9=fpm ===== 1.4 

ACFM= Vs *As 

144 

81.9 * 950400.0 

144 

540,540 ACFM 

fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

540,540 * 528 * 29.06 * 0.9921 440,019 DSCFM 

% lso.= 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (Dn)"2 

1,039 * 104.844 

625 * 29.92 

* 625 

0.9921 * 29.06 * 120 * 81.9 * 2.25000 

106.8 % 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #2 

PROJECT#: TI1550 

Run Number 

Date 

Time 

0 = Sample time 

Pb = Barometric Pressure at Port Elevation 

Vm =Vol. of Metered Gas- meter cond., cal corr. 

Tm =Meter Temperature 

Tm =Meter Temperature 

Po = Meter Orifice Pressure 

Pma = Meter Pressure Absolute 

Vtwet =Sampled Gas Volume Wet 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 

C02 =%C02,dry 

02 =%02,dry 

co =%CO,dry 

N2 = %N2,dry (N2+CO) = 1 OO-(C02+02) 

EA =Excess Air 

Vw =Volume Water 

H20 =in gas 

H20 = Moisture in Gas at Saturation 

Md =Dry Molecular Weight of Stack Gas 

Mw =Wet Molecular Weight of Stack Gas 

Psg = Stack Pressure, gauge - measured 

Psa = Stack Pressure, absolute 

1 

3/18/13 

955 - 1225 

120 

28.95 

86.540 

64.9 

524.9 

1.60 

29.07 

105.163 

84.585 

2.395 

0.40 

20.40 

0.00 

79.20 

3,469.4 

24.9 

1.37 

38.88 

28.88 

28.73 

0.10 

28.96 

2 3 

3/18/13 3/18/13 

1255 - 1505 1545 - 1800 

120 120 

28.90 28.75 

86.540 91.444 

64.9 78.4 

524.9 538.4 

1.60 1.70 

29.02 28.88 

105.711 110.383 

84.440 86.560 

2.391 2.451 

0.40 0.40 

20.40 20.50 

0.00 0.00 

79.20 79.10 

3,469.4 4,442.0 

34.3 21.3 

1.88 1.15 

38.94 52.74 

28.88 28.88 

28.68 28.76 

0.10 0.10 

28.91 28.76 

minutes 

in. Hg 

cu. ft. 

Farenheit 

Rankine 

in. H20 

in. Hg 

cu. ft. 

cu.ft 

cu. Meter 

% 

% 

% 

% 

% 

grams 

% 

% 

in. H20 

in. Hg 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #2 

PROJECT#: TI1550 

Run Number 1 2 3 

Ts = Stack Temperature 166.80 166.80 179.90 Farenheit 

Ts = Stack Temperature 347.89 347.89 355.17 Kelvin 

Ts =Stack Temperature 626.8 626.8 639.9 Rankine 

\I L1 P = A vg. Sum. of Pressure Square Root 0.02 0.02 0.02 

Vs = Velocity in the Stack 74.8 74.9 75.8 ft/min 

Vs = Velocity in the Stack 1.25 1.20 1.30 ft/sec 

As = Effective Stack Area 950,400.0 950,400.0 950,400.0 sq. m. 

Qa = Volumetric Flow Rate at stack cond. 493,680 494,340 500,280 acfm 

Qs = Volumetric Flow Rate, stand. cond., dry 397,005 394,798 392,228 dscfm 

IR = Isokinetic Ratio (Vn/Vs)* 100 95.5 95.9 98.9 % 
TEST, Inc. ~Comments: Trap #5 pah 

P AH Sampling Data 

Project# TI1550 Meter Box # 20 I Omst %C02 0.40 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.40 I 333.3 338.6 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 725.1 723.1 

Operator br Nozzle# %N2 79.20 3 746.9 748 

Run# I Nozzle Dia. (in.) 1.5 Assumed Moist % 1.22 4 606.5 609.1 

Date 3/18/13 Stack Dia.(in.) Final Moist.% 1.37 5 922.5 940.4 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic% 95.5 6 

Minlpt 5 Bar. Press. ("Hg) 28.95 Initial Leak Rate 0 cfm@ 12 "Hg 

Filter# ---- Leak Check Vol. F ina! Leak Rate 0.002 cfm@ 12 "Hg 

Dry Gas Pitot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 955 208.905 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

4-6 1000 212.260 0.0004 1.60 0.746 6.0 171 253 229 55 60 58 

5 1005 215.530 0.0004 1.60 0.746 6.0 166 260 242 54 61 60 

4 1010 219.102 0.0004 1.60 0.746 6.0 166 259 248 54 61 59 

3 1015 222.003 0.0004 1.60 0.746 6.0 169 260 251 54 61 59 

2 1020 226.202 0.0004 1.60 0.746 6.0 146 261 251 57 61 60 

1 1025 230.108 0.0004 1.60 0.746 6.0 160 265 252 58 62 61 

3-6 1035 233.418 0.0004 1.60 0.747 6.0 184 257 250 60 63 61 

5 1040 237.014 0.0004 1.60 0.747 6.0 155 256 250 58 64 62 

4 1045 241.908 0.0004 1.60 0.747 6.0 156 260 250 60 66 64 

3 1050 246.701 0.0004 1.60 0.747 6.0 149 262 250 62 69 67 

2 1055 249.309 0.0004 1.60 0.747 6.0 153 260 252 64 68 67 

1 1100 253.501 0.0004 1.60 0.747 6.0 159 265 250 65 69 68 

2-6 1110 256.403 0.0004 1.60 0.747 6.0 184 254 249 66 70 69 

5 1115 260.103 0.0004 1.60 0.747 6.0 184 255 250 66 69 67 

4 1120 263.410 0.0004 1.60 0.747 6.0 183 257 249 68 66 65 

3 1125 266.570 0.0004 1.60 0.747 6.0 178 267 250 67 64 62 

2 1130 269.601 0.0004 1.60 0.748 6.0 172 252 242 60 64 62 

1 1135 272.701 0.0004 1.60 0.748 6.0 176 260 250 57 65 63 

1-6 1200 276.608 0.0004 1.60 0.748 6.0 180 255 250 57 64 63 

5 1205 280.002 0.0004 1.60 0.748 6.0 153 255 250 55 72 70 

4 1210 283.807 0.0004 1.60 0.748 6.0 154 258 249 55 70 68 

3 1215 286.801 0.0004 1.60 0.748 6.0 168 265 250 57 70 69 

2 1220 289.704 0.0004 1.60 0.748 6.0 168 263 251 54 68 66 

1 1225 292.908 0.0004 1.60 0.748 6.0 169 264 249 54 69 68 
Example Calculations 

Run Number 

Pb 28.95 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 24.9 Water weight gain Ds 0 m. Stack Diameter 

Pm 1.6 "H20 Meter pressure As 950,400.0 Sq in. Stack Area 

Avg .!1 P 0.000 "H20 Differential pressure Dn 1.5 m Nozzle Diameter 

Avg Sqrt .!1 P 0.020 "H20 Sqrt Diff. press. 

%C02 0.40 Carbon Dioxide 

%02 20.40 Oxygen 

Vm 84.003 acf 

Ps 0.10 "H20 

Tm 64.9 (F) 

Ts 166.8 (F) 

Vmstd= 17.65*Vm*[Pb+1~] Tm(R) 

86.54 (acf * Y) 

28.96 "Hg 

524.9 (R) 

626.8 (R) 

= 17.65 * 86.540 

Tt 120 

%CO 0.00 

%N2 79.20 

Dry Gas Volume 

Stack Pressure 

Meter Temperature 

Stack Temperature 

[ 

1.60 

* 28.95 + 13.6 

524.9 } 

Vwgas = 0.0471 * Vw = 0.0471 * 24.9 1.1728 sft 3 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

84.585 sft j 

1.410 scfm 

Bws= Vwgas Bws*100 = 1.37 %Moist. Md = 28.880 

Vmstd + Vwgas 

Ts (R) 

Vs = 5129.4 * Cp * \ Ps * Mw 

5129.4 * 0.84 

1-Bws = 0.9863 

* sqrt .!1 P 

626.8 

28.96 * 28.731 * 0.020 

ACFM= Vs *As 

144 

74.8 * 950400.0 

144 

493,680 ACFM 

===== MW = 28.731 ===== 

74.8 fpm 1.25 ==== ===== fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

493,680 * 528 * 28.96 * 0.9863 

626.8 * 29.92 

397,005 DSCFM 

% Iso. = 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (Dn)"'2 

1,039 * 84.585 

0.9863 * 28.96 * 120 

* 626.8 95.5 % 

* 74.8 * 2.25000 
TEST, Inc. I Comments: Trap #8 

PAH Sampling Data 

Project# TII550 Meter Box # 20 I 0 mst %C02 0.40 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) I.0302 %02 20.40 I 339.8 350.5 

Unit/Stack Baghouse #2 Pitot Cal. (Cp) 0.84 %CO 2 703.4 70I.8 

Operator br Nozzle# %N2 79.20 3 707.7 708.7 

Run# 2 Nozzle Dia. (in.) 1.5 Assumed Moist % I.80 4 602.3 606.9 

Date 3/18/13 Stack Dia.(in.) Final Moist. % I.88 5 9I6.5 936.I 

Sample Time I20 Static Press.("H20) O.I 0 Final Isokinetic% 95.9 6 

Min/pt 5 Bar. Press. ("Hg) 28.90 Initial Leak Rate 0.001 cfm@ II "Hg 

Filter# ---- Leak Check Vol. Final Leak Rate O.OOI cfm@ II "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 1255 208.905 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

-8 1300 212.260 0.0004 1.60 0.746 6.0 17I 253 229 55 60 58 

7 1305 2I5.530 0.0004 1.60 0.746 6.0 I66 260 242 54 61 60 

6 1310 2I9.102 0.0004 1.60 0.746 6.0 I66 259 248 54 6I 59 

5 13I5 222.003 0.0004 1.60 0.746 6.0 I69 260 25I 54 61 59 

4 1320 226.202 0.0004 1.60 0.746 6.0 I46 26I 25I 57 61 60 

3 1325 230.I08 0.0004 1.60 0.746 6.0 I60 265 252 58 62 61 

2 1330 233.4I8 0.0004 1.60 0.747 6.0 I84 257 250 60 63 61 

1 1335 237.014 0.0004 1.60 0.747 6.0 I 55 256 250 58 64 62 

6-8 1345 241.908 0.0004 1.60 0.747 6.0 I 56 260 250 60 66 64 

7 1350 246.70I 0.0004 1.60 0.747 6.0 149 262 250 62 69 67 

6 1355 249.309 0.0004 1.60 0.747 6.0 I 53 260 252 64 68 67 

5 1400 253.50I 0.0004 1.60 0.747 6.0 159 265 250 65 69 68 

4 1405 256.403 0.0004 1.60 0.747 6.0 I84 254 249 66 70 69 

3 1410 260.I03 0.0004 1.60 0.747 6.0 I84 255 250 66 69 67 

2 1415 263.4IO 0.0004 1.60 0.747 6.0 I83 257 249 68 66 65 

I 1420 266.570 0.0004 1.60 0.747 6.0 I78 267 250 67 64 62 

7-8 1430 269.60I 0.0004 1.60 0.748 6.0 I72 252 242 60 64 62 

7 1435 272.70I 0.0004 1.60 0.748 6.0 I76 260 250 57 65 63 

6 1440 276.608 0.0004 1.60 0.748 6.0 I80 255 250 57 64 63 

5 I445 280.002 0.0004 1.60 0.748 6.0 I 53 255 250 55 72 70 

4 1450 283.807 0.0004 1.60 0.748 6.0 I 54 258 249 55 70 68 

3 1455 286.80I 0.0004 1.60 0.748 6.0 I68 265 250 57 70 69 

2 1500 289.704 0.0004 1.60 0.748 6.0 I68 263 25I 54 68 66 

1 1505 292.908 0.0004 1.60 0.748 6.0 169 264 249 54 69 68 
Example Calculations 

Run Number 2 

Pb 28.90 "Hg Barometric Pressure Cp 0.84 

Vw 34.3 Water weight gain Ds 0 

Pm 1.6 "H20 Meter pressure As 950,400.0 

Avg ~ P 0.000 "H20 Differential pressure Dn 1.5 

Avg Sqrt ~ P 0.020 "H20 Sqrt Diff. press. Tt 120 

%C02 0.40 Carbon Dioxide %CO 0.00 

%02 20.40 Oxygen %N2 79.20 

Vm 84.003 acf 86.54 (acf* Y) Dry Gas Volume 

Ps 0.10 "H20 28.91 "Hg Stack Pressure 

Tm 64.9 (F) 524.9 (R) Meter Temperature 

Ts 166.8 (F) 626.8 (R) Stack Temperature 

Vmstd = 17.65 * Vm * [ Pb + 1~] Tm(R) 

= 17.65 * 86.540 ·[ 1.60 

28.90 + 13.6 

524.9 } 

Vwgas = 0.0471 * Vw = 0.0471 * 34.3 1.6155 sft 3 

Pitot Cal 

m. Stack Diameter 

Sq in. Stack Area 

m Nozzle Diameter 

min Sample Time 

Carbon Monoxide 

Nitrogen 

84.440 sft j 

1.407 scfm 

Bws= Vwgas Bws* 100 = 1.88 % Moist. Md = 28.880 

Vmstd + Vwgas 

Vs = 5129.4 * 

5129.4 * 

Ts (R) 

\Ps * Mw 

0.84 

1-Bws = 0.9812 

* sqrt ~ P 

626.8 

28.91 * 28.675 * 

===== MW = 28.675 ===== 

0.020 = ==7=4.=9 = fpm ===== 1.2 

ACFM= Vs *As 

144 

74.9 * 950400.0 

144 

494,340 ACFM 

fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

494,340 * 528 * 28.91 * 0.9812 394,798 DSCFM 

% Iso.= 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (DnY'2 

1,039 * 84.44 

626.8 * 29.92 

* 626.8 

0.9812 * 28.91 * 120 * 74.9 * 2.25000 

95.9 % 
TEST, Inc. 

PAH Sampling Data 

Project# TI1550 

------- Plant Felman Productions LLC 

Unit/Stack Baghouse #2 

I Comment.: 

Meter Box# 2010 MST 

Meter Cal. (Y) 1.0302 

Pitot Cal. (Cp) 0.84 

---

%C02 0.40 

--- %02 20.50 

%CO --- Operator csm Nozzle # %N2 79.10 --- Run# 3 Nozzle Dia. (in.) 1.5 Assumed Moist% 2.00 --- ---- Date 3/18/13 Stack Dia.(in.) Final Moist.% 1.15 --- ---- Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic% 98.9 ------- --- ---

Imp. 

1 

2 

3 

4 

5 

6 

Min/pt 5 Bar. Press. ("Hg) 28.75 Initial Leak Rate 0.001 cfm@ 

Filter# Leak Check Vol. Final Leak Rate 0.001 cfm @ 

Dry Gas Pitot Orifice Vacuu Stack Probe Filter 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. 

Point 1545 401.745 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) 

8-6 1550 405.409 0.0004 1.70 0.760 6.0 194 263 244 

5 1555 409.106 0.0004 1.70 0.760 6.0 197 272 250 

4 1600 412.809 0.0004 1.70 0.760 6.0 197 263 240 

3 1605 416.760 0.0004 1.70 0.760 6.0 195 256 248 

2 1610 420.409 0.0004 1.70 0.760 6.0 197 255 250 

1 1615 423.995 0.0004 1.70 0.760 6.0 204 258 253 

9-6 1625 427.603 0.0004 1.70 0.760 6.0 174 270 248 

5 1630 431.201 0.0004 1.70 0.760 6.0 177 272 251 

4 1635 434.902 0.0004 1.70 0.760 6.0 178 254 250 

3 1640 438.608 0.0004 1.70 0.747 6.0 180 256 250 

2 1645 442.406 0.0004 1.70 0.747 7.0 176 255 250 

1 1650 446.001 0.0004 1.70 0.747 7.0 172 259 250 

10-6 1700 449.809 0.0004 1.70 0.747 7.0 167 258 250 

5 1705 453.302 0.0004 1.70 0.747 7.0 180 258 251 

4 1710 457.106 0.0004 1.70 0.747 7.0 151 258 251 

3 1715 460.804 0.0004 1.70 0.747 7.0 180 260 249 

2 1720 464.409 0.0004 1.70 0.747 7.0 180 261 250 

1 1725 468.209 0.0004 1.70 0.747 7.0 179 260 251 

11-6 1735 471.908 0.0004 1.70 0.747 7.0 171 270 249 

5 1740 475.650 0.0004 1.70 0.747 7.0 164 265 249 

4 1745 479.303 0.0004 1.70 0.747 7.0 173 258 250 

3 1750 483.005 0.0004 1.70 0.747 7.0 175 258 250 

2 1755 486.707 0.0004 1.70 0.747 7.0 179 262 251 

1 1800 490.508 0.0004 1.70 0.747 7.0 177 261 250 

Initial Final 

339.4 344.7 

725.6 721.8 

747.8 746.5 

607.8 612.8 

940.4 956.5 

12 "Hg 

14 "Hg 

Imp. Dry Gas 

Temp. Temp. 

(F) In Out 

65 69 68 

67 70 70 

67 72 70 

66 76 74 

65 78 77 

63 79 78 

60 80 78 

63 80 77 

63 81 80 

65 81 79 

66 82 80 

66 82 81 

60 81 80 

52 80 78 

54 80 78 

53 80 79 

52 81 80 

52 83 81 

53 81 80 

48 81 79 

49 80 78 

49 81 80 

50 81 78 

50 81 80 
Example Calculations 

Run Number 3 

Pb 28.75 "Hg Barometric Pressure Cp 0.84 

Vw 21.3 Water weight gain Ds 0 

Pm 1.7 "H20 Meter pressure As 950,400.0 

Avg ~ P 0.000 "H20 Differential pressure Dn 1.5 

Avg Sqrt ~ P 0.020 "H20 Sqrt Diff. press. Tt 120 

%C02 0.40 Carbon Dioxide %CO 0.00 

%02 20.50 Oxygen 

Vm 88.763 acf 

Ps 0.10 "H20 

Tm 78.4 (F) 

Ts 179.9 (F) 

Vmstd = 17.65 * Vm * [ Pb + l~J Tm(R) 

%N2 79.10 

91.444 (acf* Y) Dry Gas Volume 

28.76 "Hg Stack Pressure 

538.4 (R) Meter Temperature 

639.9 (R) Stack Temperature 

~ 17.65 • 91.444 • [ 28.75 + .L1Q 13.6 ]= -

538.4 

Vwgas = 0.0471 * Vw = 0.0471 * 21.3 1.0032 sft 3 

Pitot Cal 

m. Stack Diameter 

Sq in. Stack Area 

m Nozzle Diameter 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

86.560 sft j 

1.443 scfm 

Bws= Vwgas Bws*lOO = 1.15 %Moist. Md = 28.884 ===== Vmstd + Vwgas 1-Bws = 0.9885 MW = 28.759 

Ts(R) 

Vs= 5129.4 * Cp * \Ps * Mw * sqrt ~ P 

639.9 

5129.4 * 0.84 28.76 * 28.759 * 0.020 ===7=5.=8=fpm 

ACFM= Vs *As 

144 

75.8 * 950400.0 

144 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

% Iso.= 1039 * Vmstd * Ts (R) 

(1-Bws) * Ps * Tt * Vs * (Dn)l'2 

1,039 * 86.56 

0.9885 * 28.76 * 120 

500,280 ACFM 

500,280 * 528 * 28.76 * 0.9885 

639.9 * 29.92 

* 639.9 98.9 % 

* 75.8 * 2.25000 

===1=.3==fps 

392,228 DSCFM 
EXAMPLE CALCULATIONS 

HYDROGEN CHLORIDE 

mgHCl 24.04 Hydrogen Chloride ppm = x ---

Vmstd (cu.m) 36.45 

HCllbslhr = mg HCl x __ l..::g._r- x DSCFM x 60 min llb 

X 

Vmstd 64.8 mg 1 hr 7,000 gr 

36.45 = Molecular Weight of Hydrogen Chloride 

24.04 = L~ .?al G<.'S CoEslant liters/g-mole 

DSCFM* = Stack Flow Rate 

Vmstd* = Volume of dry gas sampled at standard 

conditions dry standard cubic feet 

Vmstd* (cu.m) = Volume of dry gas sampled (cubic meters) 

* 29.92 "Hg, 68 degrees F (760 mm Hg, 20 degrees C) 
EXAMPLE CALCULi\TIONS 

MERCURY 

lbs/hr=--m-=g- x --1-=g"-r- x DSCFM x 

Vmstd 64.8 mg 

DSCFM* = Stack Flow Rate 

60min 

lhr 

Vmstd* = Volume of dry gas sampled at standard 

conditions dry standard cubic feet 

* 29.92 "Hg, 68 degrees F (760 mm Hg, 20 degrees C) 

llb 

x---

7,000 gr 
EXAMPLE CALCULATIONS 

11ULTIPLE ~\1ETALS 

mg 1 gr lbs/hr = ----"'"- X _ _____,......__ X DSCFM X 

Vmstd 64.8 mg 

DSCFM* = Stack Flow Rate 

60min 

lhr 

Vmstd* = Volume of dry gas sampled at standard 

conditions dry standard cubic feet 

* 29.92 "Hg, 68 degrees F (760 mm Hg, 20 degrees C) 

1 lb 

x---

7,000 gr 
APPENDIXB 

PRE-FLOW DATA 
TEST, Inc. ~Comments: 

Method SD Setup ~----------------------------------------~ Project# Meter Box# 2010 MST %C02 0.01 Imp. Initial Final ----- Plant Meter Cal. (Y) 1.0283 %02 20.80 1 703.7 695 

Unit/Stack Pitot Cal. (Cp)_0_.8_4 __ %CO ----- 2 711.3 723.5 

Operator Nozzle# %N2 79.19 3 597.8 601.3 ---- Run# BH2 Inlet Nozzle Dia. (in.) Assumed Moist% 1.15 4 896.3 908.3 ----- ----- Date 3/12/13 Stack Dia.(in.) 144 Final Moist.% 1.15 5 ----- Sample Time 30 Static Press.("H20) -0.40 Final Isokinetic % #REF! 6 ------------ Min/pt 5 Bar. Press. ("Hg) 28.95 Initial Leak Rate 0.006 cfm @ 14 "Hg 

Filter# Leak Check Vol. Final Leak Rate 0.006 cfm@ 14 "Hg 

Dry Gas Pitot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 163.555 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

236.550 0.40 1.20 0.628 2.0 358 40 40 

0.42 355 

0.45 353 

0.45 352 

0.40 356 

0.38 366 

0.35 363 

0.33 365 

0.32 361 

0.28 350 

0.26 344 

0.25 345 

0.50 368 

0.52 374 

0.53 372 

0.53 373 

0.50 370 

0.46 372 

0.45 374 

0.40 368 

0.30 368 

0.27 363 

0.24 362 

0.22 341 
Example Calculations 

Run Number BH2 Inlet 

Pb 28.95 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 19 Water weight gain Ds 144 in. Stack Diameter 

Pm 1.2 "H20 Meter pressure As 16,286.0 Sq in. Stack Area 

Avg /'). P 0.384 "H20 Differential pressure Dn 0 m Nozzle Diameter 

Avg Sqrt /'). P 0.614 "H20 Sqrt Diff. press. Tt 30 min Sample Time 

%C02 0.01 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.80 Oxygen 

Vm 72.995 acf 

Ps -0.40 "H20 

Tm 40.0 (F) 

Ts 361.4 (F) 

Vmstd = 17.65 * Vm * [ Pb + 1~] Tm{R) 

Vwgas = 0.0471 * Vw = 0.0471 * 

Bws= Vwgas 

V mstd + Vwgas 

Ts (R) 

Vs = 5129.4 * Cp * \ Ps * Mw 

5129.4 * 0.84 

75.061 (acf* Y) 

28.92 "Hg 

500 (R) 

821.4 (R) 

= 17.65 * 75.061 

%N2 79.19 

Dry Gas Volume 

Stack Pressure 

Meter Temperature 

Stack Temperature 

·[ 1.20 

28.95 + 13.6 

500.0 } 

Nitrogen 

76.941 sft 5 

1.282 scfm 

19 0.8949 sft 3 

Bws*100 = 1.15 %Moist. Md = 28.834 ===== 1-Bws = 0.9885 MW = 28.709 ===== 

* sqrt /'). P 

821.4 

28.92 * 28.709 * 0.614 = 2,631.4 fpm 43.86 ====== 

ACFM= Vs *As 

144 

2,631.4 * 16286.0 

144 

297,604 ACFM 

fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

297,604 * 528 * 28.92 * 0.9885 

821.4 * 29.92 

182,781 DSCFM 
Method 5D Velocity Calculation 

Area of measurement site Ao= 

Temp. at measurement site To= 

Ambient temp. Tarnb = 

Inlet temp. Ti = 

Inlet gas volume flow rate Qi= 

Eq. SD-3 Dilution Air Flow Rate 

Qd = Qi (Ti-To) 

To-Tarnb 

Qd = 5239.722 (DSCFS) 

Eq. SD-2 Volumetric Flow Rate 

Qo = Qi+Qd 

Qo = 8286.072 (DSCFS) 

Eq. SD-1 Average Gas Velocity 

Qo v =--=:._- Ao 

v= 1.255465 (FPS) 

6600)ft2 

155f (F) 615 ( R) 

35) (F) 495 ( R) 

361.4 (F) 821.4 (R) 

182,781 (DSCFM) 3046.35 (DSCFS) 
ISOKINETIC PRELIMINARY SETUP CALCULATIONS 

%Moisture 1.15 % Y= 1.0283 

Md = 0.9885 ll p = 0.000413 "H20 

C02 0.01 % \Ill p = 0.020 "H20 

02 20.80 % Pb 28.95 "Hg 

co = % Cp 0.84 

N2 79.19 % Ts 155 OF 615 

MWd 28.834 Tm = 40 OF 500 

MW 28.709 (28.966) Psa = -0.400 "H20 28.92 

AssumedRm 

Assumed Tt 

Assumedcf = 

Velocity Calculation 

Vs = 

= 

\Ill 

ll 

Nozzle Diameter 

Dn = 

= 

Meter Rate 

Rm 

0.650 (0.60-0.85) cfm 

120 mm 

78.0 (scfm * Tt) 

85.49. Cp. llllP • \I(MW. ~:,) 

( 61.8044 *\Ill p ) = 1.2555 fps 

p = 0.02031 

p = 0.000413 

Rm * Ts * Y 

\ 0.33 * V s * Tm * Md 

Desired 1.397 in Actual 1.500 in 

0.33 * (Vs * \(A""i>'") * Tm * Md * Dn 2 

Ts* Y 

0.729 cfm cf * Tt = 87.42 cf 

Correction factor = cfm 

\Ill p 

35.865 @ 40 

Rate Correction Multipliers 

= Rm(new)= Tm(new) + 460 

Tm( old) + 460 

35.865 * \Ill P ® __ 4_o __ 

36.582 * \Ill P ® __ 5_o __ 

37.299 * \Ill P ® __ 6_o __ 

* Rm(old) 

°FTm 

°FTm 

°FTm 

OR 

OR 

"Hg 
38.017 *\lAp @ 70 °FTm 

38.734 *\lAp @ 80 °FTm 

39.451 *\lAp @ 90 °FTm 

40.169 *\lAp @ 100 °FTm 

40.886 *\lAp @ 110 °FTm 
TEST, Inc. 'Comments: 

Method 5D Setup 

Project# Meter Box# 2010 MST %C02 0.01 Imp. Initial Final 

Plant Meter Cal. (Y) 1.0283 %02 20.80 1 703.7 695 

Unit/Stack Pitot Cal. (Cp) 0.84 %CO 2 711.3 723.5 

Operator Nozzle# %N2 79.19 3 597.8 601.3 

Run # BH2 Inlet Nozzle Dia. (in.) Assumed Moist % 1.15 4 896.3 908.3 

Date 3/12/13 Stack Dia.(in.) 144 Final Moist. % 1.15 5 

Sample Time 30 Static Press.("H20) -0.40 Final lsokinetic% #REF! 6 

Min/pt 5 Bar. Press. ("Hg) 28.95 Initial Leak Rate 0.006 cfm@ 14 "Hg 

Filter# Leak Check Vol. Final Leak Rate 0.006 cfm@ 14 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 163.555 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

236.550 0.50 1.20 0.628 2.0 375 40 40 

0.50 375 

0.52 395 

0.52 398 

0.50 395 

0.45 395 

0.42 396 

0.43 389 

0.43 385 

0.42 384 

0.37 382 

0.26 365 

0.55 399 

0.50 404 

0.47 399 

0.44 403 

0.43 398 

0.44 405 

0.40 407 

0.32 408 

0.30 402 

0.28 397 

0.26 395 

0.26 390 
Example Calculations 

Run Number BH2 Inlet 

Pb 28.95 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 19 Water weight gain Ds 144 m. Stack Diameter 

Pm 1.2 "H20 Meter pressure As 16,286.0 Sq in. Stack Area 

Avg !). P 0.415 "H20 Differential pressure Dn 0 m Nozzle Diameter 

A vg Sqrt !). P 0.641 "H20 Sqrt Diff. press. Tt 30 

%C02 0.01 Carbon Dioxide %CO 0.00 

%02 20.80 Oxygen 

Vm 72.995 acf 

Ps -0.40 "H20 

Tm 40.0 (F) 

Ts 393.4 (F) 

Vmstd = 17.65 * Vm * [ Pb + 1r::,J 

Tm(R) 

Vwgas = 0.0471 * Vw = 0.0471 * 

75.061 (acf* Y) 

28.92 "Hg 

500 (R) 

853.4 (R) 

= 17.65 * 75.061 

%N2 79.19 

Dry Gas Volume 

Stack Pressure 

Meter Temperature 

Stack Temperature 

·[ 1.20 

28.95 + 13.6 

500.0 } 

19 0.8949 sft 3 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

76.941 sft j 

1.282 scfm 

Bws= Vwgas Bws*100 = 1.15 %Moist. Md = 28.834 

Vmstd + Vwgas 

Ts (R) 

Vs = 5129.4 * Cp * \ Ps * Mw 

==== 1-Bws = 0.9885 

* sqrt !). P 

5129.4 * 0.84 I 853.4 

* \ -2-8-.9-2--*--2-8-. 7-0-9 * 

===== MW = 28.709 ===== 

0.641 = 2,800.1 fpm 46.67 ====== 

ACFM= Vs *As 

144 

2,800.1 * 16286.0 

144 

316,684 ACFM 

fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

316,684 * 528 * 28.92 * 0.9885 

853.4 * 29.92 

187,206 DSCFM 
Method 5D Velocity Calculation 

Area of measurement site Ao= 

Temp. at measurement site To= 

Ambient temp. Tamb= 

Inlet temp. Ti = 

Inlet gas volume flow rate Qi= 

Eq. SD-3 Dilution Air Flow Rate 

Qd = Qi (Ti-To) 

To-Tamb 

Qd = 5971.313 (DSCFS) 

Eq. SD-2 Volumetric Flow Rate 

Qo = Qi+Qd 

Qo = 9091.413 (DSCFS) 

Eq. SD-1 Average Gas Velocity 

Qo v =----"--

Ao 

v= 1.377487 (FPS) 

. 6600}ft2 

158! (F) 618 ( R) 

35}(F) 495 ( R) 

393.4 (F) 853.4 ( R) 

187,206 (DSCFM) 3120.1 (DSCFS) 
ISOKINETIC PRELIMINARY SETUP CALCULATIONS 

%Moisture 

Md 

C02 = 

02 

co 

N2 = 

MWd 

MW 

AssumedRm 

Assumed Tt 

Assumedcf = 

Velocity Calculation 

Vs 

\IL\ 

L\ 

Nozzle Diameter 

Dn = 

1.15 % Y= 1.0283 

0.9885 L\ p = 0.000494 "H20 

0.01 % \IL\ p = 0.022 "H20 

20.80 % Pb 28.95 "Hg 

% Cp = 0.84 

79.19 % Ts = 158 OF 618 

28.834 Tm = 40 OF 500 

28.709 (28.966) Psa = -0.400 "H20 28.92 

0.650 (0.60-0.85) cfm 

120 mm 

78.0 (scfm * Tt) 

85.49 • Cp • \ld p • \I(MW • ~:.,) 

( 61.9550 * \IL\ p ) = 1.3775 fps 

p 0.02223 

p 0.000494 

Rm * Ts * Y 

\ 0.33 * Vs * Tm * Md 

= Desired 1.337 in Actual 1.500 in 

Meter Rate 

Rm= 0.33 * (Vs * \~) * Tm * Md * Dn 2 

Ts* Y 

= 0.795 cfm cf* Tt= 95.46 cf 

Correction factor = cfm 

\IL\ p 

35.778 @ 40 

Rate Correction Multipliers 

Rm(new)= Tm(new) + 460 * Rm(old) 

Tm( old) + 460 

35.778 * \IL\ p ® 40 °FTm 

36.493 * \IL\ p ® 50 °FTm 

37.209 * \IL\ p ® 60 °FTm 

OR 

OR 

"Hg 
37.924 *'I~ p ® 70 °FTm 

38.640 * \1~ p @ 80 °FTm 

39.355 * \1~ p @ 90 °FTm 

40.071 * \1~ p @ 100 °FTm 

40.786 * \1~ p @ 110 °FTm 
TEST, Inc. I Comments: 

Method 5D Setup 

Project# Meter Box # 2010 MST %C02 0.01 Imp. Initial Final 

Plant Meter Cal. (Y) 1.0283 %02 20.80 1 703.7 695 

Unit/Stack Pitot Cal. (Cp) 0.84 %CO 2 711.3 723.5 

Operator Nozzle# %N2 79.19 3 597.8 601.3 

Run # BH2 Inlet Nozzle Dia. (in.) Assumed Moist % 1.15 4 896.3 908.3 

Date 3/12/13 Stack Dia.(in.) 144 Final Moist. % 1.13 5 

Sample Time 30 Static Press.("H20) -0.40 Final Isokinetic% #REF! 6 

Min/pt 5 Bar. Press. ("Hg) 28.95 Initial Leak Rate 0.006 cfm@ 14 "Hg 

Filter# Leak Check Vol. Final Leak Rate 0.006 cfm@ 14 "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 163.555 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

236.550 0.50 1.20 0.628 2.0 406 30 30 

0.48 408 

0.47 407 

0.44 411 

0.44 412 

0.43 412 

0.42 412 

0.40 410 

0.33 404 

0.24 392 

0.20 380 

0.21 398 

0.50 405 

0.47 402 

0.44 402 

0.42 408 

0.40 407 

0.40 410 

0.40 412 

0.38 411 

0.35 409 

0.26 406 

0.23 389 

0.24 372 
Example Calculations 

Run Number BH2 Inlet 

Pb 28.95 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 19 Water weight gain Ds 144 in. Stack Diameter 

Pm 1.2 "H20 Meter pressure As 16,286.0 Sq in. Stack Area 

Avg ~ P 0.377 "H20 Differential pressure On 0 m Nozzle Diameter 

Avg Sqrt ~ P 0.609 "H20 Sqrt Diff. press. Tt 30 mm Sample Time 

%C02 0.01 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.80 Oxygen 

Vm 72.995 acf 

Ps -0.40 "H20 

Tm 30.0 (F) 

Ts 403.5 (F) 

Vmstd = 17.65 * Vm * [ Pb + 1~] Tm(R) 

Vwgas = 0.0471 * Vw = 0.0471 * 

Bws= Vwgas 

Vmstd + Vwgas 

Ts (R) 

Vs = 5129.4 * Cp * \ Ps * Mw 

5129.4 * 0.84 

75.061 (acf* Y) 

28.92 "Hg 

490 (R) 

863.5 (R) 

=17.65 * 75.061 

%N2 79.19 

Dry Gas Volume 

Stack Pressure 

Meter Temperature 

Stack Temperature 

·[ 1.20 

28.95 + 13.6 

490.0 } 

Nitrogen 

78.511 sft j 

1.309 scfm 

19 0.8949 sft 3 

Bws*100 = 1.13 %Moist. Md = 28.834 ===== 1-Bws = 0.9887 MW = 28.712 ===== 

* sqrt ~ P 

863.5 

28.92 * 28.712 * 0.609 = 2,675.9 fpm 44.60 ===== 

ACFM= Vs *As 

144 

2,675.9 * 16286.0 

144 

302,637 ACFM 

fps 

DSCFM = ACFM * 528 * Ps * (1-Bws) 

Ts (R) * 29.92 

302,637 * 528 * 28.92 * 0.9887 

863.5 * 29.92 

176,846 DSCFM 
Method 5D Velocity Calculation 

Area of measurement site Ao= 

Temp. at measurement site To= 

Ambient temp. Tamb= 

Inlet temp. Ti = 

Inlet gas volume flow rate Qi= 

Eq. SD-3 Dilution Air Flow Rate 

Qd = Qi (Ti-To) 

To-Tamb 

Qd = 5882.885 (DSCFS) 

Eq. SD-2 Volumetric Flow Rate 

Qo = Qi+Qd 

Qo = 8830.319 (DSCFS) 

Eq. SD-1 Average Gas Velocity 

Qo v=-~-

Ao 

v= 1.337927 (FPS) 

6600)ft2 

158J (F) 618 ( R) 

351 (F) 495 ( R) 

403.5 (F) 863.5 ( R) 

176,846 (DSCFM) 2947.433 (DSCFS) 
ISOKINETIC PRELIMINARY SETUP CALCULATIONS 

%Moisture 

Md 

C02 

02 

co 

N2 = 

MWd 

MW 

AssumedRm 

Assumed Tt 

Assumed cf = 

Velocity Calculation 

Vs 

\1.1 

.1 

Nozzle Diameter 

Dn = 

= 

Meter Rate 

Rm 

1.13 % Y= 1.0283 

0.9887 .1 p = 0.000466 "H20 

0.01 % \1.1 p = 0.022 "H20 

20.80 % Pb 28.95 "Hg 

% Cp 0.84 

79.19 % Ts = 158 OF 618 

28.834 Tm 30 OF 490 

28.711 (28.966) Psa = -0.400 "H20 28.92 

0.650 (0.60-0.85) cfm 

240 mm 

156.0 (scfm * Tt) 

85.49 • cp • llt.r • \I(Mw • ~:,.l 

( 61.9526 * \1.1 p ) = 1.3379 fps 

p = 0.02160 

p = 0.000466 

Rm * Ts * Y 

\ 0.33 * Vs * Tm * Md 

Desired 1.3 70 in Actual 1.500 in 

0.33 * (Vs * \(A"i>") * Tm * Md * Dn 2 

Ts* Y 

0.757 cfm cf * Tt = 181.76 cf 

Correction factor= cfm 

\1.1 p 

35.068 @ 30 

Rate Correction Multipliers 

Rm(new)= Tm(new) + 460 

Tm( old) + 460 

35.068 * \1.1 p @ __ 3_0 --

35.783 * \1.1 p @ __ 4_0 __ 

36.499 * \1.1 p @ __ 5_0 --

* Rm(old) 

°FTm 

°FTm 

°FTm 

OR 

OR 

"Hg 
37.215 *\lAp @ 60 °FTm 

37.930 *\lAp @ 70 °FTm 

38.646 *\lAp @ 80 °FTm 

39.362 *\lAp @ 90 °FTm 

40.077 *\lAp @ 100 °FTm 
APPENDIXC 

ANALYTICAL DATA 

'I 
Run 

Number 

1 

2 

3 

ANALYTICAL RESULTS 

Filter 

Number 

1007 

1006 

1005 

Particulate Matter 

Felman Productions LLC 

Baghouse#2 

Filter Acetone Rinse 

Final Weight Final Weight 

(grams) (grams) 

0.0008 0.0043 

0.0004 0.0038 

0.0003 0.0045 

Total 

Particulate 

Matter 

(grams) 

0.0051 

0.0042 

0.0048 
_·.·'\ Lab Conditions ,, ) > .i ·1 . Filter Gravimetric Analysis Temperature: 18 oc 

Bar. Press.: 29.03 "Hg 

Project Number: TI1550 Location: Baghouse #2 

Company: Felman Productions LLC EPA Method: 5 Analyst: JPS 

Initial Tray Filter Tare Tray/Filter 

Weight Weight Weight Weight Results 

Filter Number: 1007 Number Date Time .(gl .(gl .(gl .(gl 

Notes: 1 4115/2013 800 0.9230 0.5558 1.4796 0.0008 

2 4/15/2013 1200 0.9230 0.5558 1.4796 0.0008 

3 4/15/2013 1600 0.9230 0.5558 1.4796 0.0008 - Final Weight: 0.0008 

Initial Tray Filter Tare Tray/Filter 

Weight Weight Weight Weight Results 

Filter Number: 1006 Number Date Time .(gl .(gl .(gl .(gl 

Notes: 1 4/15/2013 800 0.9230 0.5567 1.4801 0.0004 

2 4/15/2013 1200 0.9230 0.5567 1.4802 0.0005 

3 4115/2013 1600 0.9230 0.5567 1.4801 0.0004 

Final Weight: 0.0004 

Initial Tray Filter Tare Tray/Filter 

Weight Weight Weight Weight Results 

Filter Number: 1005 Number Date Time .(gl .(gl .(gl .(gl 

Notes: 1 4115/2013 800 0.9230 0.5282 1.4515 0.0003 

2 4115/2013 1200 0.9230 0.5282 1.4515 0.0003 

3 4/15/2013 1600 0.9230 0.5282 1.4515 0.0003 

Final Weight: 0.0003 
~ Inc,. Rinse Gravimetric Analysis 

Project Number: TI1550 

---------------- Lab Conditions 

Company: Felman Productions LLC Temperature: 18 °C ------------

Location: Baghouse #2 Bar. Press.: 29.03 "Hg 

Analyst: JPS 

----------------

Initial Beaker Beaker/Sample Final 

Filter Beaker Weight Weight Weight 

Number Number Date Time {g} {g} {g} 

1007 2-1 4/15/2013 800 102.9716 102.9759 0.0043 

1006 2-2 4/15/2013 800 95.7555 95.7593 0.0038 

1005 2-3 4115/2013 800 106.8597 106.8642 0.0045 
Your P.O.#: 10244 

Your Project#: Tl1550 

Attention: Lorri L White 

Keika Ventures 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your C.O.C. #: NA 

Chapel Hill 

101 Strangford Lane 

Durham, NC 

USA 27713 

Report Date: 2013/04/18 

CERTIFICATE OF ANALYSIS 

MAXXAM JOB#: 8351189 

Received: 2013/04/06, 13:00 

Sample Matrix: Stack Sampling Train 

#Samples Received: 8 

Analyses 

Hydrogen Halides in H2S04 Imp. 

Volume of Sulfuric Acid lmpinger 

Quantity 

8 

8 

Date 

Extracted 

2013/04/12 

N/A 

Date 

Analyzed Laboratory Method 

2013/04/12 BRL SOP-00108 

2013/04/12 

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

Ancy Sebastian 

vttb~..__ 18 Apr 201311:13:25-04:00 

Encryption Key E 

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

Ancy Sebastian, C. Tech., Senior Project Manager, Air Taxies 

Email: ASebastian@maxxam.ca 

Phone# (905) 817-5831 

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

Method 

Reference 

EPA Method 26A 

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

5.1 0.2 of ISO/IEC 17025:2005(E), signing the reports. For Service Group specific validation please refer to the Validation Signature Page. 

Maxxam Analytics Inc. is a NELAC accredited laboratory. Certificate# CANA001. Use of the NELAC logo however does not insure that 

Maxxam is accredited for all of the methods indicated. This certificate shall not be reproduced except in full, without the written approval of 

Maxxam Analytics Inc. Maxxam has procedures in place to guard against improper use of the electronic signature and have the required 

"signatories", as per section. 

Total cover pages: 1 

Page 1 of7 

1\!1axxarn /\na!ytics International Corporation o/a Maxxam Analytics 6740 Campobello Road. Mtssissauga, Ontario, LSN 2L8 Tel: (905} 817~5700 Toll-free: BOD-563-6266 Fax: (905} 817-5777 v1vvw.maxxam.ca 
Ma-62am 

Maxxam Job #: 8351189 

Report Date: 2013/04/18 

Maxxam ID 

~ampling Date 

r.oc Number 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

RC1306 RC1307 RC1308 RC1309 

2013/03/27 2013/03/27 2013/03/19 2013/03/19 

00:01 00:01 00:01 00:01 

NA NA NA NA 

Units ~LANK-H2S04-M26A BLANK-H20·M26A RUN RUN RDL QC Batch 

1·BAGH 2·M26A 2·BAGH 2·M26A 

Sulfuric Acid Volume ml 325 354 360 409 1 3179578 

Hydrochloric Acid ug <200 <200 3100 2500 200 3179677 

RDL = Reportable Detection Limit 

QC Batch = Quality Control Batch 

Maxxam ID RC1310 RC1311 RC1312 RC1313 

Sampling Date 2013/03/19 2013/03/15 2013/03/15 2013/03/15 

00:01 00:01 00:01 00:01 

COC Number NA NA NA NA 

Units RUN RUN RUN RUN RDL QC Batch 

3-BAGH 2·M26A 1·BAGH 5·M26A 2·BAGH 5·M26A 3·BAGH 5·M26A 

Sulfuric Acid Volume ml 379 390 357 406 1 3179578 

Hydrochloric Acid ug 1900 230 <200 <200 200 3179677 

RDL = Reportable Detection Limit 

QC Batch = Quality Control Batch 

Page2 of7 

l\ila,xam l•nalytics lrnernational COrporalion o/a Maxxam Anal~'lics 6740 Canpobello Road, M!SSissauga, omario, L5N 2LB Tel: (905) 817-5700 Toll-Free: 800-563·6266 Fax: (905) 817-5777 www.maxxam.ca 
MaO-am 

Keika Ventures 

Maxxam Job #: 8351189 Client Project #: Tl1550 

Report Date: 2013/04/18 Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

Test Summary 

Maxxam ID RC1306 Collected 2013/03/27 

Sample ID BLANK-H2S04-M26A Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

ICISPEC 3179677 2013104/12 

3179578 N/A 

Maxxam ID RC1307 Collected 2013103127 

Sample ID BLANK-H20-M26A Shipped 

Matrix Stack Sampling Train Received 2013/04106 

Instrumentation Batch Extracted 

ICISPEC 3179677 2013104112 

3179578 N/A 

Maxxam ID RC1308 Collected 2013/03/19 

Sample ID RUN 1-BAGH 2-M26A Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

IC/SPEC 3179677 2013/04/12 

3179578 N/A 

Maxxam ID RC1308 Dup Collected 2013/03/19 

Sample ID RUN 1-BAGH 2-M26A Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

IC/SPEC 3179677 2013/04/12 2013/04112 Ann-Marie Stern 

Maxxam ID RC1309 Collected 2013/03/19 

Sample ID RUN 2-BAGH 2-M26A Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

IC/SPEC 3179677 2013104/12 2013/04/12 Ann-Marie Stem 

3179578 N/A 2013/04/12 

Maxxam ID RC1310 Collected 2013/03/19 

Sample ID RUN 3-BAGH 2-M26A Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

IC/SPEC 3179677 2013/04/12 

3179578 N/A 

Page 3 of? 

Maxxam Analylics lrnernatlonal COrporation o/a Maxxam Analytics 6740 C<mpoDello Road, Mlsslssauga, Ontario, L5N 2L8 Tel: (905) 817-5700 TOll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
l\11 a({}la m 

Maxxam Job #: 8351189 

Report Date: 2013/04/18 

Maxxam ID RC1311 

Sample ID RUN 1-BAGH 5-M26A 

Matrix Stack Sampling Train 

Maxxam ID RC1312 

Sample ID RUN 2-BAGH 5-M26A 

Matrix Stack Sampling Train 

Maxxam ID RC1313 

Sample ID RUN 3-BAGH 5-M26A 

Matrix Stack Sampling Train 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

Test Summary 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Instrumentation Batch Extracted 

IC/SPEC 3179677 2013/04/12 

3179578 N/A 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Instrumentation Batch Extracted 

IC/SPEC 3179677 2013/04/12 

3179578 N/A 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Instrumentation Batch Extracted 

IC/SPEC 3179677 2013/04/12 

3179578 N/A 

Page4 of? 

Ma<Xam Analylics lrnernational COrporation ola Maxxam Anal~"'ics 6740 CampobeHo Road, Mlsslssauga, Ontario, L5N 2L8 Tel: (905) 817·5700 Toll-Free: 800·563-6266 Fax: (90s) 817·5777 www.maxxam.ca 
Ma"62-am 

Maxxam Job #: 8351189 

Report Date: 2013/04/18 

Results relate onlv to the items tested. 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

GENERAL COMMENTS 

Page5of7 

1\i!a"xam Analylics lrrternational COrporation o/a Maxxam Analytlcs 6740 C<mpobeno Road, Mlsslssauga, OntariO, L5N 2L8 Tel: (905) 817-5700 Toll-Free: SOQ-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
QA/QC 

Batch 

Num lnit QC Tvoe Parameter 

3179677 A_S Matrix Spike 

(RC1308) Hydrochloric Acid 

Spiked Blank Hydrochloric Acid 

Method Blank Hydrochloric Acid 

RPDSample/Sample 

Duo Hydrochloric Acid 

Keika Ventures 

Attention: Lorri L White 

Client Project#: Tl1550 

P.O.#: 10244 

Site Location: TEST INC. ~ FELMAN PRODUCTIONS 

Quality Assurance Report 

Maxxam Job Number: GB351189 

Date 

Analyzed 

vvvv/mm/dd 

2013/04/12 

2013/04/12 

2013/04/12 

2013/04/12 

Value %Recoverv 

100 

102 

<200 

0.2 

Units 

% 

% 

ug 

% 

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

QC Limits 

•' 

80-120 

90- 110 

20 

Spiked Blank: A blank matrix sample to which a known amount of the analyte, usually from a second source, has been added. Used to evaluate method 

!accuracy. 

Method Blank: A blank matrix containing all reagents used in the analytical procedure. Used to identify laboratory contamination. 

Page 6 of7 

1\ilaxxam AnalyUcs lmernational COrporation o!a Maxxam Analyllcs 6740 campobello Road, Mlsslssauga, OntariO, L5N 2L8 Tel: (905) 817·5700 Toll-free: 800.563·6266 Fax: (905) 817·5777 www.maxxam.ca 
Ma?_{)2am 

Validation Signature Page 

Maxxam Job #: 8351189 

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 5.1 0.2 of 

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

Page? of? 

Ma:<xam Analytics International Corporation o/a Maxxam Anal}'lics 6740 Campobello Road, MlssiSsauga, Ontario, L5N 2L8 Tel: (905) 817·5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
M.r-3?{)2am 

Attention: Lorri L White 

Keika Ventures 

Chapel Hill 

101 Strangford Lane 

Durham, NC 

USA 27713 

Your P.O.#: 10244 

Your Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Report Date: 2013/04/17 

CERTIFICATE OF ANALYSIS 

MAXXAM JOB#: 8351214 

Received: 2013/04/06, 13:00 

Sample Matrix: Stack Sampling Train 

# Samples Received: 7 

Analyses 

Metals in Combined Train (6020) 

Date Date Method 

Quantity Extracted Analyzed Laboratory Method Reference 

7 2013/04/10 2013/04/12 BRL SOP-00103/ BRL EPA 6020 I M29 

SOP-00102 

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

Ancy Sebastian 

m£1>\.- 17 Apr 201314:33:19 -{J•I:OO 

Encryption KeyE 

Please direct all qu ""v"" '"Y"''u'"Y '"'"Certificate of Analysis to your Project Manager. 

Ancy Sebastian, C. Tech., Senior Project Manager, Air Toxics 

Email: ASebastian@maxxam.ca 

Phone#(905)817-5831 

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

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. 

Maxxam Analytics Inc. is a NELAC accredited laboratory. Certificate # CANA001. Use of the NELAC logo however does not insure that 

Maxxam is accredited for all of the methods indicated. This certificate shall not be reproduced except in full, without the written approval of 

Maxxam Analytics Inc. Maxxam has procedures in place to guard against improper use of the electronic signature and have the required 

"signatories", as per section. 

Total cover pages: 1 

Page 1 of8 

1\ila,xam Analytics International COrporation o/a Maxxam Anal~>tics 6740 GampobeRo Road, Mlssissauga, OnlariO, L5N 21..8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
J\/1 a ({)2 a m 

Maxxam Job #: 8351214 

Report Date: 2013/04/17 

Maxxam ID 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

ELEMENTS BY ICP/MS (STACK SAMPLING TRAIN) 

RC1448 RC1449 RC1450 RC1451 

Sampling Date 2013/03/27 2013/03/13 2013/03/13 2013/03/13 

00:01 00:01 00:01 00:01 

Units BLANK-M29 RDL RUN RUN RUN RDL 

1-BAGH 2-M29 2-BAGH 2-M29 3-BAGH 2-M29 

Combined Train Arsenic (As) ug <0.40 0.40 <2.0 <2.0 <2.0 2.0 

Combined Train Cadmium (Cd) ug <0.10 0.10 <0.50 <0.50 <0.50 0.50 

Combined Train Chromium (Cr) ug 1.80 0.30 3.9 11.4 6.5 1.5 

Combined Train Lead (Pb) ug 0.84 0.20 50.0 25.0 28.3 1.0 

Combined Train Manganese (Mn) ug 8.25 0.75 3370 976 1280 3.8 

Combined Train Nickel (Ni) ug 1.69 0.50 4.7 11.1 9.1 2.5 

RDL = Reportable Detection Limit 

QC Batch = Quality Control Batch 

Maxxam ID RC1452 RC1453 RC1454 

Sampling Date 2013/03/13 2013/03/13 2013/03/13 

00:01 00:01 00:01 

Units RUN RUN RUN RDL QC Batch 

1-BAGH 5-M29 2-BAGH 5-M29 3-BAGH 5-M29 

Combined Train Arsenic (As) ug <2.0 <2.0 <2.0 2.0 3177251 

Combined Train Cadmium (Cd) ug <0.50 <0.50 <0.50 0.50 3177251 

Combined Train Chromium (Cr) ug 7.4 38.3 3.6 1.5 3177251 

Combined Train Lead (Pb) ug 25.9 36.2 14.0 1.0 3177251 

Combined Train Manganese (Mn) ug 607 547 400 3.8 3177251 

Combined Train Nickel (Ni) ug 5.7 14.7 4.3 2.5 3177251 

RDL = Reportable Detection Limit 

QC Batch = Quality Control Batch 

Page 2 of8 

pc Batch 

3177251 

3177251 

3177251 

3177251 

3177251 

3177251 

Ma«am AnalyUcs lrnernational COrporation O!a Maxxam Analy·rics 6740 campobello Road, Mlssissauga, Ontario, L5N 2LB Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fa>:: (905) 817-5777 www.maxxam.r.a 
M a ({52 am 

Keika Ventures 

Maxxam Job #: 8351214 Client Project #: Tl1550 

Report Date: 2013/04/17 Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

Test Summary 

Maxxam ID RC1448 Collected 2013/03/27 

Sample ID BLANK-M29 Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

ICP1/MS 3177251 2013/04/10 

Maxxam ID RC1449 Collected 2013/03/13 

Sample ID RUN 1-BAGH 2-M29 Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

ICP1/MS 3177251 2013/04/10 

Maxxam ID RC1449 Dup Collected 2013/03/13 

Sample ID RUN 1-BAGH 2-M29 Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

ICP1/MS 3177251 2013/04/10 2013/04/12 Nan Ra kha 

Maxxam ID RC1450 Collected 2013/03/13 

Sample ID RUN 2-BAGH 2-M29 Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

ICP1/MS 3177251 2013/04/10 2013/04/12 Nan Ra kha 

Maxxam ID RC1451 Collected 2013/03/13 

Sample ID RUN 3-BAGH 2-M29 Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

ICP1/MS 3177251 2013/04/10 

Maxxam ID RC1452 Collected 2013/03/13 

Sample ID RUN 1-BAGH 5-M29 Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

ICP1/MS 3177251 2013/04/10 

Maxxam ID RC1453 Collected 2013/03/13 

Sample ID RUN 2-BAGH 5-M29 Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

ICP1/MS 3177251 2013/04/10 

Page 3 of8 

Ma-.am P.nalylics lrrternational COrporation o/a Maxxam Anal~'tics 6740 CampobeUo Road, Mlsslssauga, omario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: BOQ-563-6266 Fax: (905) 817-5777 \YWW.maxxam.ca 
Maxxam Job #: 8351214 

Report Date: 2013/04/17 

Maxxam ID RC1454 

Sample ID RUN 3-BAGH 5-M29 

Matrix Stack Sampling Train 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

Test Summary 

Collected 2013/03/13 

Shipped 

Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

ICP1/MS 3177251 2013/04/10 2013/04/12 Nan Ra kha 

Page4 of 8 

f\ilaxxam AnalyHcs Jnternalional Corporation o/a Maxxam Analytics 6740 Campobello Road, Mlssissauga, Ontario, L5N 2l8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 W\VW.maxxam.ca 
f\/1 a ?.{)2 a m 

Maxxam Job #: 8351214 

Report Date: 2013/04/17 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

ELEMENTS BY ICP/MS (STACK SAMPLING TRAIN) 

Metals in Combined Train (6020): Extra 5x dilution was required for all samples except RC1448, due to the matrix 

Post digestion duplicate and spike was done on sample RC1449. 

Results relate onlv to the items tested. 

Page5of8 

Mauam AnalyUcs lrnernatlonal COrporation o/a Maxxam Analytlcs 6740 C<mpobello Road, M!Sslssauga, omarlo, L5N 2L8 Tel: (905) 817•5700 Toll-Free: 800.563·6266 Fax: (905) 817·5777 www.maxxam.ca 
Ma{!52am 

QA/QC 

Batch 

Num lnit QC Type 

3177251 N_R Matrix Spike 

(RC1449) 

MS/MSD RPD 

Matrix Spike 

(RC1449) 

MS/MSD RPD 

Matrix Spike 

(RC1449) 

MS/MSDRPD 

Matrix Spike 

(RC1449) 

MS/MSD RPD 

Matrix Spike 

(RC1449) 

MS/MSD RPD 

Matrix Spike 

(RC1449) 

MS/MSD RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Method Blank 

RPD 

Method Blank 

RPD 

Method Blank 

RPD 

Method Blank 

RPD 

Method Blank 

RPD 

Method Blank 

RPD 

RPDSample/Sample 

Dup 

Keika Ventures 

Attention: Lorri L White 

Client Project #: Tl1550 

P.O.#: 10244 

Site Location: TEST INC. -FELMAN PRODUCTIONS 

Quality Assurance Report 

Maxxam Job Number: GB351214 

Date 

Analyzed 

Parameter yyyy/mm/dd 

Combined Train Arsenic (As) 2013/04/12 

Combined Train Arsenic (As) 2013/04/12 

Combined Train Cadmium (Cd) 2013/04/12 

Combined Train Cadmium (Cd) 2013/04/12 

Combined Train Chromium (Cr) 2013/04/12 

Combined Train Chromium (Cr) 2013/04/12 

Combined Train Lead (Pb) 2013/04/12 

Combined Train Lead (Pb) 2013/04/12 

Combined Train Manganese (Mn) 2013/04/12 

Combined Train Manganese (Mn) 2013/04/12 

Combined Train Nickel (Ni) 2013/04/12 

Combined Train Nickel (Ni) 2013/04/12 

Combined Train Arsenic (As) 2013/04/12 

Combined Train Arsenic (As) 2013/04/12 

Combined Train Cadmium (Cd) 2013/04/12 

Combined Train Cadmium (Cd) 2013/04/12 

Combined Train Chromium (Cr) 2013/04/12 

Combined Train Chromium (Cr) 2013/04/12 

Combined Train Lead (Pb) 2013/04/12 

Combined Train Lead (Pb) 2013/04/12 

Combined Train Manganese (Mn) 2013/04/12 

Combined Train Manganese (Mn) 2013/04/12 

Combined Train Nickel (Ni) 2013/04/12 

Combined Train Nickel (Ni) 2013/04/12 

Combined Train Arsenic (As) 2013/04/12 

Combined Train Arsenic (As) 2013/04/12 

Combined Train Cadmium (Cd) 2013/04/12 

Combined Train Cadmium (Cd) 2013/04/12 

Combined Train Chromium (Cr) 2013/04/12 

Combined Train Chromium (Cr) 2013/04/12 

Combined Train Lead (Pb) 2013/04/12 

Combined Train Lead (Pb) 2013/04/12 

Combined Train Manganese (Mn) 2013/04/12 

Combined Train Manganese (Mn) 2013/04/12 

Combined Train Nickel (Ni) 2013/04/12 

Combined Train Nickel (Ni) 2013/04/12 

Combined Train Arsenic (As) 2013/04/12 

Combined Train Cadmium (Cd) 2013/04/12 

Combined Train Chromium (Cr) 2013/04/12 

Combined Train Lead (Pb) 2013/04/12 

Combined Train Manganese (Mn) 2013/04/12 

Combined Train Nickel (Nil 2013/04/12 

Value %Recovery 

98 

7.4 

103 

6.0 

104 

5.9 

109 

7.6 

126 

13.6 

105 

6.9 

98 

6.1 

99 

7.2 

98 

5.4 

102 

5.9 

101 

5.4 

101 

6.6 

<0.40 

NC 

<0.10 

NC 

<0.30 

NC 

<0.20 

NC 

<0.75 

NC 

<0.50 

NC 

NC 

NC 

NC 

2.3 

1.4 

NC 

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

Units 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

% 

ug 

% 

ug 

% 

ug 

% 

ug 

% 

ug 

% 

ug 

% 

% 

% 

% 

% 

% 

% 

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

QC Limits; 

70 -13~ 20 

70-130 

20 

70-130 

20 

70-130 

20 

70- 130 

20 

70- 130 

20 

85- 115 

20 

85- 115 

20 

85-115 

20 

85-115 

20 

85-115 

20 

85- 115 

20 

20 

20 

20 

20 

20 

20 

20 

20 

20 

20 

20 

20 

Spiked Blank: A blank matrix sample to which a known amount of the analyte, usually from a second source, has been added. Used to evaluate method 

accuracy. 

Method Blank: A blank matrix containing all reagents used in the analytical procedure. Used to identify laboratory contamination. 

Page 6 of8 

Mauam AnalyUcs lrrternational COrporation o/a Maxxam Analytics 6740 GampobeHo Road, MISSiSsauga, Ontario, L5N as Tel: (905) 817·5700 Toll-Free: 81)()-563·6266 Fa>:: (905) 817-5777 www.maxxam.ca 
Ma?§f.am 

Keika Ventures 

Attention: Lorri L White 

Client Project #: Tl1550 

P.O.#: 10244 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Quality Assurance Report (Continued) 

Maxxam Job Number: GB351214 

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 7 of8 

Ma.xam Analytics !rtternauonal corporation Ola Maxxam Analytlcs 6740 campolleHo Rosa, Mtsslssauga, Ontarlo,l5N as Tel: (905) 817-5700 Ton-Free: 800-563-6266 Fax: (9Q5) 817-5777 www.maxxam.ca 
Ma[{)2am 

Validation Signature Page 

Maxxam Job #:8351214 

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. 

Page8of8 

1\flaxxam Anatylics trnernattonal COrporation o/a Maxxam Analytlcs 6740 Campobello Road, MISsiSsauga, Ontario, LSN 2LB Tel: (905) 817-5700 Toll-Free: aoo-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
- ~rFI'' ~~· ,:·.¥' ............,.. .. · ~' -JJ~<·6 

If: <,~'fa '~ . ~~:e,.l11~ ~ljlir -

~·"" 

.I V"l!m' ~ ...!lJI~, 

rbent Trap Analysis Report 

3nt Name Keika Ventures, LLC 

act Name Lorri White 

=tp J.D. Plant/Source Date Analyzed Scientist 

156035 Felman 4/10/2013 John Perko 

150823 Felman 4/10/2013 John Perko 

156060 Felman 4/10/2013 John Perko 

156021 Felman 4/10/2013 John Perko 

156066 Felman 4/10/2013 John Perko 

156064 Felman 4/10/2013 John Perko 

156014 Felman 4/10/2013 John Perko 

150797 Felman 4/10/2013 John Perko 

156042 Felman 4/10/2013 John Perko 

156034 Felman 4/10/2013 John Perko 

156058 Felman 4/10/2013 John Perko 

156006 Felman 4/10/2013 John Perko 

156057 Felman 4/10/2013 John Perko 

156069 Felman 4/10/2013 John Perko 

150824 Felman 4/10/2013 John Perko 

'-- -----·---------·-

s than 0.027 ng is considered"< LDL." Which is less than the lowest 

detection limit. 

:~tion Report Available -------~==--=1 iliti±10%J 

Massng 

Sect.1 

0.86 

21.06 

0.67 

0.65 

0.51 

0.73 

0.65 

21.20 

0.61 

19.31 

17.28 

28.22 

26.06 

22.55 

45.09 

-~~---·-··---

Ohio Lumex Co., Inc. 

9263 Ravenna Rd., Unit A-3 

Twinsburg, OH 44087 

Phone: (330) 405-0837 

Fax: (330) 405-0847 

vvww.ohiolumexcom 

Turn -Around Time 

~~~~:J Standard 

D 48 hour rush 

Other 

Project Number 2001307 

Date ________ 4/11/2013 _ 

Phone 919-933-9569 

Mass ng Mass ng Spike BreakSect.2 Sect.3 Level (ng) through% Comme1 

0.74 FiE 

0.54 20 Trc: 

0.54 Trc: 

0.61 #5 Baghouse 

0.52 #5 Baghouse 

0.74 #5 Baghouse 

0.55 #5 Baghouse 

0.74 20 #5 Baghouse 

0.47 #5 Baghouse 

0.72 #2 Baghouse 

0.72 #2 Baghouse 

0.87 #2 Baghouse 

0.72 #2 Baghouse 

0.73 #2 Baghouse 

0.57 20 #2 Baghouse 

--------~------ -·------- ---- ----~------------- --
Ma?§i.am 

Your P.O.#: 10244 

Your Project #: Tl1550 

Attention: Lorri L White 

Keika Ventures 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

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

Chapel Hill 

101 Strangford Lane 

Durham, NC 

USA 27713 

Report Date: 2013/04/29 

CERTIFICATE OF ANALYSIS 

MAXXAM JOB#: 8351227 

Received: 2013/04/06, 13:00 

Sample Matrix: Stack Sampling Train 

# Samples Received: 7 

Analyses 

2,3,7,8-TCDF Confirmation (M23) 

Dioxins/Furans in Air (Method 23) 

PCB Congeners in Air (1668A) 

Quantity 

6 

7 

7 

Date 

Extracted 

N/A 

2013/04/16 

2013/04/16 

Date 

Analyzed Laboratory Method 

2013/04/24 BRL SOP-00404 

2013/04/25 BRL SOP-00404 

2013/04/24 BRL SOP-00408, 409 

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

Ancy Sebastian 

~~rd.~ 29 Apr 2013 23:03:49 .04:00 

Encryption Key~ 

Please direct all qu "'"v""' '"!ofo•u•"l:l .,,;:; Certificate of Analysis to your Project Manager. 

Ancy Sebastian, C.Tech., Senior Project Manager, Air Toxics 

Email: ASebastian@maxxam.ca 

Phone# (905) 817-5831 

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

Method 

Reference 

EPA1613Bmod(M23/23A) 

EPA1613Bmod(M23/23A) 

EPA 1668A (0010) mod 

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

5.1 0.2 of ISO/IEC 17025:2005(E), signing the reports. For Service Group specific validation please refer to the Validation Signature Page. 

Maxxam Analytics Inc. is a NELAC accredited laboratory. Certificate # CANA001. Use of the NELAC logo however does not insure that 

Maxxam is accredited for all of the methods indicated. This certificate shall not be reproduced except in full, without the written approval of 

Maxxam Analytics Inc. Maxxam has procedures in place to guard against improper use of the electronic signature and have the required 

"signatories", as per section. 

Total cover pages: 1 

Page 1 of29 

1\<la.Xxam Analylics International COrporation o/a Maxxam Analytics 6740 Gampobello Road, Mtssissauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: BOQ-563·6266 Fax: (905) 817-5777 www.maxxam.ca 
Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1495 

~ampling Date 2013/03/15 

00:01 

roc Number N/A TOXIC EQUIVALENCY 

Units TRAIN EDL ~DL TEF (2005 WHO) TEQ(DL) 

BLANK·M23/PCB 

33'44'-TetraCB-(77) ng 1.4 0.037 0.30 0.00010 0.00014 

344'5-TetraCB-(81) ng 0.081 ~.038 0.30 0.00030 0.000024 

233'44'-PentaCB-(105) ng 1.4 0.032 0.30 0.000030 0.000042 

2344'5-PentaCB-(114) ng 0.12 0.030 0.30 0.000030 0.0000036 

23'44'5-PentaCB-(118) ng 3.9 0.032 0.30 0.000030 0.00012 

23'44'5'-PentaCB-( 123) ng 0.073 0.034 0.30 0.000030 0.0000022 

33'44'5-PentaCB-( 126) ng <0.031 0.031 0.30 0.10 0.0031 

HexaCB-(156)+(157) ng 0.17 ~.033 0.60 0.000030 0.0000051 

23'44'55'-HexaCB-(167) ng 0.069 0.035 0.30 0.000030 0.0000021 

33'44'55'-HexaCB-( 169) ng <0.037 0.037 0.30 0.030 0.0011 

233'44'55'-HeptaCB-(189) ng <0.030 ~.030 0.30 0.000030 0.00000090 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.0045 

Surrogate Recovery(%) 

C 13-233'44'55'-HeptaCB-( 189) % 96 N/A N/A N/A N/A 

C 13-233'44'5-HexaCB-( 156) % 107 N/A N/A N/A N/A 

C 13-233'44'5'-HexaCB-( 157) o/o 107 N/A N/A N/A N/A 

C13-233'44'-PentaCB-(1 05) o/o 117 N/A N/A N/A N/A 

C13-23'44'55'-HexaCB-( 167) o/o 104 N/A N/A N/A N/A 

C13-2344'5-PentaCB-(114) o/o 114 N/A N/A N/A N/A 

C13-23'44'5-PentaCB-(118) o/o 113 N/A N/A N/A N/A 

C13-2'344'5-PentaCB-(123) o/o 113 N/A N/A N/A N/A 

~13-33'44'55'-HexaCB-(169) o/o 97 N/A N/A N/A N/A 

C 13-33'44'5-PentaCB-( 126) o/o 117 N/A N/A N/A N/A 

C13-33'44'-TetraCB-(77) o/o 119 N/A N/A N/A N/A 

C 13-344'5-TetraCB-(81 ) o/o 119 N/A N/A N/A N/A 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

#of 

somers 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

~c Batch 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

N/A 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

WH0(2005): The 2005 World Health Organization. Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 2 of29 

Ma:<xam Ana!ylics !rnernational COrporation a/a Maxxam Analytics 6740 Campollello Road. Mlssissauga. Ontario. L5N 2'-8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 \YWW.maxxam.c.a 
rv1c:t"§am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1497 

Sampling Date 2013/03/19 

00:01 

OC Number N/A TOXIC EQUIVALENCY 

Units RUN EDL RDL TEF (2005 WHO) TEQ(DL) 

1·BH2·M23/PCB 

33'44'-TetraCB-(77) ng 4.3 0.036 0.30 0.00010 0.00043 

344'5-TetraCB-(81) ng 0.26 0.037 0.30 0.00030 0.000078 

233'44'-PentaCB-(105) ng 4.4 0.033 0.30 0.000030 0.00013 

2344'5-PentaCB-( 114) ng 0.36 0.031 0.30 0.000030 0.000011 

23'44'5-PentaCB-(118) ng 12 0.033 0.30 0.000030 0.00036 

23'44'5'-PentaCB-(123) ng 0.23 0.035 0.30 0.000030 0.0000069 

33'44'5-PentaCB-( 126) ng 0.081 0.032 0.30 0.10 0.0081 

HexaCB-(156)+(157) ng 0.46 0.029 0.60 0.000030 0.000014 

~3'44'55'-HexaCB-(167) ng 0.18 0.031 0.30 0.000030 0.0000054 

33'44'55'-HexaCB-(169) ng <0.033 0.033 0.30 0.030 0.00099 

233'44'55'-HeptaCB-(189) ng <0.028 0.028 0.30 0.000030 0.00000084 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.010 

Surrogate Recovery (%) 

C13-233'44'55' -HeptaCB-( 189) % 95 N/A N/A N/A : N/A --· ... 

C 13-233'44 '5-HexaC:B-{15Fl ~10 10fl . ',1·!'., N/A f\:''' N/A ;--------------------~---- -·-r----······ ----· ·-·---

C13-23:::"<;..+'5'-hex<,. '-·· ::,; J I % 1 i ..... ·::: N/A N/A N/A N/A 

C13-233'44'-PentaCB-(105) % 114 N/A N/A N/A N/A 

C 13-23'44'55'-HexaCB-( 167) % 107 N/A N/A N/A N/A 

C13-2344'5-PentaCB-(114) % 118 N/A N/A N/A N/A 

C 13-23'44'5-PentaCB-( 118) % 116 N/A N/A N/A N/A 

C13-2'344'5-PentaCB-(123) % 115 N/A N/A N/A N/A 

C13-33'44'55'-HexaCB-(169) % 106 N/A N/A N/A N/A 

C 13-33'44'5-PentaCB-( 126) % 117 N/A N/A N/A N/A 

C 13-33'44'-TetraCB-(77) % 121 N/A N/A N/A N/A 

C13-344'5-TetraCB-(81) % 115 N/A N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

TEF = Toxic Equivalency Factor, TEO = Toxic Equivalency Quotient, 

#of 

somers pc Batch 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A N/A 

' ' 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

The Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

~H0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 3 of 29 

Ma:<xam Analylics lrnemational Corporation o!a Maxxam Anal~'lics 6740 campobello Road, Mlssissauga, Ontario, L5111 2LB Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
rvra;:{)iam 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1498 

~ampling Date 2013/03/19 

00:01 

toe Number N/A TOXIC EQUIVALENCY 

Units RUN EDL RDL [TEF (2005 WHO) TEQ(DL) 

2-BH2-M23/PCB 

33'44'-TetraCB-(77) ng 2.6 0.036 0.30 0.00010 0.00026 

344'5-TetraCB-(81) ng 0.15 0.036 0.30 0.00030 0.000045 

233'44'-PentaCB-(105) ng 2.5 0.031 0.30 0.000030 0.000075 

2344'5-PentaCB-(114) ng 0.20 0.029 0.30 0.000030 0.0000060 

23'44'5-PentaCB-(118) ng 6.7 0.031 0.30 0.000030 0.00020 

23'44'5'-PentaCB-(123) ng 0.11 0.033 0.30 0.000030 0.0000033 

33'44'5-PentaCB-(126) ng 0.048 0.030 0.30 0.10 0.0048 

HexaCB-(156)+(157) ng 0.25 0.034 0.60 0.000030 0.0000075 

23'44'55'-HexaCB-(167) ng 0.11 0.036 0.30 0.000030 0.0000033 

33'44'55'-HexaCB-( 169) ng <0.037 0.037 0.30 0.030 0.0011 

233'44'55'-HeptaCB-( 189) ng <0.023 0.023 0.30 0.000030 O.OC000069 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.0065 

Surrogate Recovery (%) 

C13-233"44'55'-HeptaCB-I1 &91 ~-~, 97 N/.A NIA N_,., ~'-!',A. 

.. -· --··.-·---· ---

·c l3-233'44'!.)'Rr-:t·,~-!~i~-(_, ~-., 1 '1o 110 I. r• '•'<iA Ni"- :·,,A 

C13-233'44'-PentaCB-(105) % 113 N/A N/A N/A N/A 

C13-23'44'55'-HexaCB-(167) % 106 N/A N/A N/A N/A 

C13-2344'5-PentaC5-\ ·: i..1 .· : ~'c ; 

I 

~: 13 ; N/A ~i/A N/f- NIA 

·-·-- --·--------·- C13-23'44'5-PentaCB-(118) % 113 N/A N/A N/A N/A 

C13-2'344'5-PentaCB-(123) % 111 N/A N/A N/A N/A 

C 13-33'44'55'-HexaCB-( 169) % 106 N/A N/A N/A N/A 

C13-33'44'5-PentaCB-( 126) % 117 N/A N/A N/A N/A 

C13-33'44'-TetraCB-(77) % 115 N/A N/A N/A N/A 

C13-344'5-TetraCB-(81) % 115 N/A N/A N/A N/A 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

TEF = Toxic Equivalency Factor, TEO = Toxic Equivalency Quotient, 

#of 

somers ~c Batch 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A N/A 

~ .. ,: :' :::. .: ... ?::50F 

~ .. -...... ..: . --·"'"":3Ct) 

N/A 3182506 

N/A 3182506 

; 

~-1/,.'! I 2"!0:':'7~-f-': 

---

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

The Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 4 of29 

Ma:<xam Analytics rrnernational COrporation o/a Maxxam Analytics 6740 campobello Road. Mlssissauga. Ontario. L5N 2L8 Tel: (905) 817-5700 Toll-Free: aoo-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma({)2am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1499 

~ampling Date 2013/03/19 

00:01 

OC Number N/A TOXIC EQUIVALENCY 

Units RUN EDL fRDL rrEF (2005 WHO) TEQ(DL) 

3-BH2-M23/PCB 

33'44'-TetraCB-(77) ng 1.5 0.038 0.30 0.00010 0.00015 

344'5-TetraCB-(81) ng 0.085 O.Q38 0.30 0.00030 0.000026 

233'44'-PentaCB-(105) ng 1.4 0.032 0.30 0.000030 0.000042 

2344'5-PentaCB-( 114) ng 0.12 0.030 0.30 0.000030 0.0000036 

~3'44'5-PentaCB-(118) ng 3.9 0.032 0.30 0.000030 0.00012 

23'44'5'-PentaCB-(123) ng 0.082 0.034 0.30 0.000030 0.0000025 

33'44'5-PentaCB-( 126) ng 0.033 ~.031 0.30 0.10 0.0033 

HexaCB-( 156)+( 157) ng 0.17 0.035 0.60 0.000030 0.0000051 

23'44'55'-HexaCB-( 167) ng 0.068 0.038 0.30 0.000030 0.0000020 

33'44'55'-HexaCB-(169) ng <0.039 0.039 0.30 0.030 0.0012 

233'44'55'-HeptaCB-(189) ng <0.023 0.023 0.30 0.000030 0.00000069 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.0049 

Surrogate Recovery(%) i "' 

C 13-233'44 '55'-HeptaCB-( 189) % 94 IN/A N/A N/A N/A 

C13-233'44'5-HexaCB-(156) % 102 N/A N/A N/A N/A 

C13-233'44'5'-HexaCB-(157) % 102 N/A N/A N/A N/A 

C 13-233'44 '-PentaCB-( 1 05) % 109 N/A N/A N/A N/A 

C13-23'44'55'-HexaCB-(167) % 100 N/A N/A N:A NiA 

C13-2344'5-PentaCB-(114) % 106 N'A N/A N'A N/A 

C13-23'44'5-PentaCB-(118) % 105 N/A N/A N/A N/A 

C13-2'344'5-PentaCB-(123) % 103 N/A N/A N/A N/A 

lc13-33'44'55'-HexaCB-(169) % 90 N/A N/A N/A N/A 

C13-33'44'5-PentaCB-(126) % 113 N/A N/A N/A N/A 

C13-33'44'-TetraCB-(77) % 110 N/A N/A N/A N/A 

C 13-344'5-TetraCB-(81) % 111 N/A N/A N/A N/A 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

#of 

somers pc Batch 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A N/A 

- NIA 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182:0•'3 

N/A 318250·3 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

N/A 3182506 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 5 of29 

! 

I 

Ma'Xam Analy!iGs !mernational COrporation o!a Maxxam Anal~'tics 6740 Campobello Road, Mtssissauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1500 

Sampling Date 2013/03/15 

00:01 

OC Number N/A TOXIC EQUIVALENCY 

Units RUN EDL RDL TEF (2005 WHO) TEQ{DL} 

1-BH5-M23/PCB 

33'44'-TetraCB-(77) ng 5.2 0.039 0.30 0.00010 0.00052 

344'5-TetraCB-(81) ng 0.31 0.040 0.30 0.00030 0.000093 

233'44'-PentaCB-(1 05) ng 5.4 0.031 0.30 0.000030 0.00016 

2344'5-PentaCB-(114) ng 0.42 0.030 0.30 0.000030 0.000013 

23'44'5-PentaCB-(118) ng 15 0.031 0.30 0.000030 0.00045 

23'44'5'-PentaCB-(123) ng 0.31 0.033 0.30 0.000030 0.0000093 

33'44'5-PentaCB-(126) ng 0.10 0.031 0.30 0.10 0.010 

HexaCB-( 156)+( 157) ng 0.52 0.033 0.60 0.000030 0.000016 

23'44'55'-HexaCB-( 167) ng 0.22 0.036 0.30 0.000030 0.0000066 

33'44'55'-HexaCB-(169) ng <0.037 0.037 0.30 0.030 0.0011 

~33'44'55'-HeptaCB-( 189) ng <0.026 0.026 0.30 0.000030 0.00000078 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.012 

Surrogate Recovery {%) 

C 13-233'44'55'-HeptaCB-( 189) % 94 N/A N/A N/A N/A 

C 13-233'44'5-HexaCB-( 156) % 110 N/A N/A N/A N/A 

C 13-233'44 '5'-HexaCB-( 157) % 110 N/A N/A N/A N/A 

C13-233'44'-PentaCB-( 1 05) % 112 N/A N/A N/A N/A 

C13-23'44 '55'-HexaCB-( 167) % 107 N/A N/A N/A N/A 

C 13-2344'5-PentaCB-( 114) % 115 N/A N/A N/A N/A 

C13-23'44'5-PentaCB-(118) % 115 N/A N/A N/A N/A 

C13-2'344'5-PentaCB-(123) % 114 N/A N/A N/A N/A 

C 13-33'44'55'-HexaCB-{ 169) % 111 N/A N/A N/A N/A 

~13-33'44'5-PentaCB-(126) % 123 N/A N/A N/A N/A 

C13-33'44'-TetraCB-(77) % 123 N/A N/A N/A N/A 

C13-344'5-TetraCB-(81) % 117 N/A N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

~EF =Toxic Equivalency Factor, TEQ =Toxic Equivalency Quotient, 

#of 

somers 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

pc Batch 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

N/A 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins snd 

Dioxin-like Compounds 

Page 6 of29 

i 

1\ilaxxaon Analylics InternatiOnal COrporation ola Maxxam Anal~'lics 5740 C<mpobello Road, MISSiSsauga. OntariO, LSN 21..8 Tel: (905) 817-5700 Toll-Free: aoo-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Maxxam Job #:8351227 

Report Date: 2013/04/29 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1505 

Sampling Date 2013/03/15 

00:01 

OC Number N/A TOXIC EQUIVALENCY 

Units RUN EDL RDL TEF (2005 WHO) TEQ(DL) 

2·BH5-M23/PCB 

33'44'-TetraCB-(77) ng 8.4 0.037 0.30 0.00010 0.00084 

344'5-TetraCB-(81) ng 0.48 O.Q38 0.30 0.00030 0.00014 

233'44'-PentaCB-( 1 05) ng 8.3 ~.036 0.30 0.000030 0.00025 

2344'5-PentaCB-(114) ng 0.69 0.034 0.30 0.000030 0.000021 

23'44'5-PentaCB-(118) ng 23 0.036 0.30 0.000030 0.00069 

23'44'5'-PentaCB-(123) ng 0.32 ~.038 0.30 0.000030 0.0000096 

33'44'5-PentaCB-(126) ng 0.16 ~.035 0.30 0.10 0.016 

HexaCB-(156)+(157) ng 0.76 ~.032 0.60 0.000030 0.000023 

23'44'55'-HexaCB-( 167) ng 0.32 O.D35 0.30 0.000030 0.0000096 

33'44'55'-HexaCB-(169) ng <0.036 ~.036 0.30 0.030 0.0011 

233'44'55'-HeptaCB-( 189) ng <0.029 0.029 0.30 0.000030 0.00000087 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.019 

Surrogate Recovery (%) 

C13-233'44'55'-HeptaCB-(189) % 101 N/A N/A N/A N/A 

C13-233'44'5-HexaCB-(156) % 120 N/A N/A N/A N/A 

C13-233'44'5'-HexaCB-(157) % 120 N/A N/A N/A N/A 

C13-233'44'-PentaCB-(105) % 121 N/A N/A N/A N/A 

C13-23'44'55'-HexaCB-(167) % 120 N/A N/A N/A N/A 

C13-2344'5-PentaCB-( 114) % 130 N/A N/A N/A N/A 

C13-23'44'5-PentaCB-(118) % 129 N/A N/A N/A N/A 

C 13-2'344'5-PentaCB-( 123) % 129 N/A N/A N/A N/A 

C 13-33'44'55'-HexaCB-(169) % 113 N/A N/A N/A N/A 

C13-33'44'5-PentaCB-( 126) % 136 N/A N/A N/A N/A 

C13-33'44'-TetraCB-(77) % 137 N/A N/A N/A N/A 

C13-344'5-TetraCB-(81) % 127 N/A N/A N/A N/A 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

#of 

somers 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

QC Batch 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

N/A 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

WvH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxin~ and 

Dioxin-like Compounds 

Page 7 of29 

·• 

Maxxam Analytics lrnernational COrporation o/a Maxxam Analytics 6740 CampobeHo R<>att, Mlsslssauga. Onlario, L5N 2LB Tel: (905) 817·5700 Toll-Free: BOQ-563-6266 Fax: (905) 817·5777 www.maxxam.r.a 
Ma§am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1511 

~ampling Date 2013/03/15 

00:01 

toe Number N/A TOXIC EQUIVALENCY 

Units RUN EDL RDL TEF (2005 WHO) TEQ{DL) 

3-BH5-M23/PCB 

33'44'-TetraCB-(77) ng 6.6 0.054 0.30 0.00010 0.00066 

344'5-TetraCB-(81) ng 0.42 ~.055 0.30 0.00030 0.00013 

233'44'-PentaCB-(105) ng 6.2 ~.037 0.30 0.000030 0.00019 

2344'5-PentaCB-(114) ng 0.51 0.035 0.30 0.000030 0.000015 

23'44'5-PentaCB-(118) ng 17 0.038 0.30 0.000030 0.00051 

23'44'5'-PentaCB-(123) ng 0.34 0.039 0.30 0.000030 0.000010 

33'44'5-PentaCB-(126) ng 0.17 0.037 0.30 0.10 0.017 

HexaCB-(156)+(157) ng 0.60 0.036 0.60 0.000030 0.000018 

23'44'55'-HexaCB-(167) ng 0.23 0.038 0.30 0.000030 0.0000069 

33'44'55'-HexaCB-( 169) ng <0.040 0.040 0.30 0.030 0.0012 

233'44'55'-HeptaCB-( 189) ng <0.030 0.030 0.30 0.000030 0.00000090 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.020 

Surrogate Recovery (%) 

C 13-233'44'55'-HeptaCB-( 189) % 95 N/A N/A N/A N/A 

C13-233'44'5-HexaCB-( 156) % 114 N/A N/A N/A N/A 

C13-233'44'5'-HexaCB-(157) % 114 N/A N/A N/A N/A 

C13-233'44'-PentaCB-(105) % 113 N/A N/A N/A N/A 

C13-23'44'55'-HexaCB-(167) % 112 N/A N/A N/A N/A 

C13-2344'5-PentaCB-(114) % 118 N/A N/A N/A N/A 

C13-23'44'5-PentaCB-(118) % 119 N/A N/A N/A N/A 

C 13-2'344'5-PentaCB-( 123) % 114 N/A N/A N/A N/A 

C 13-33'44'55'-HexaCB-(169) % 110 N/A N/A N/A N/A 

C13-33'44'5-PentaCB-( 126) % 124 N/A N/A N/A N/A 

C13-33'44'-TetraCB-(77) % 121 N/A N/A N/A N/A 

C 13-344'5-TetraCB-(81) % 112 N/A N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

#of 

somers 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

N/A 

~EF = Toxic Equivalency Factor, TEO = Toxic Equivalency Quotient, 

~he Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

QC Batch 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

N/A 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

3182506 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dic>:'ns E~c 

Dioxin-like Compounds 

Page8of29 

1\!laxxam AnalyUcs lrnernational COrporatiOn o/a Maxxam Analytics 6740 C<mpObeHo Roao, MISSissauga, Ontario, L5N 2l.S Tel: (905) 817-5700 Toll-Free: SOQ-563-6266 Fax: (905) 817-5777 W\V'N.maxxam.ca 
Ma?_(lam 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

Sampling Date 

COC Number 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS {STACK SAMPLING TRAIN) 

RC1495 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units TRAIN EDL RDL TEF (2005 WHO) fEQ(DL) somers 

BLANK-M23/PCB 

2,3,7,8-Tetra COD* pg <3.7 3.7 30 1.00 3.70 N/A 

1,2,3,7,8-Penta COD pg <7.7 7.7 30 1.00 7.70 N/A 

1 ,2,3,4,7,8-Hexa COD pg <5.3 5.3 30 0.100 0.530 N/A 

1 ,2,3,6,7,8-Hexa COD pg <5.2 5.2 30 0.100 0.520 N/A 

1,2,3,7,8,9-Hexa COD pg <5.2 5.2 30 0.100 0.520 N/A 

1 ,2,3,4,6, 7,8-Hepta COD pg <6.4 6.4 30 0.0100 0.0640 N/A 

1,2,3,4,6,7,8,9-0cta COD pg 8.2 (1) 5.2 300 0.000300 0.00246 N/A 

Total Tetra COD pg <3.7 3.7 30 N/A N/A N/A 

Total Penta COD pg <7.7 7.7 30 N/A N/A N/A 

Total Hexa COD pg <5.2 5.2 30 N/A N/A N/A 

Total Hepta COD pg <6.4 6.4 30 N/A N/A N/A 

2,3,7,8-Tetra CDF ** pg <2.5 2.5 30 0.100 0.250 N/A 

1,2,3,7,8-Penta CDF pg <7.6 7.6 30 0.0300 0.228 N/A 

2,3,4,7,8-Penta CDF pg <7.2 7.2 30 0.300 2.16 N/A 

1,2,3,4,7,8-Hexa CDF pg <3.9 3.9 30 0.100 0.390 N/A 

1 ,2,3,6,7,8-Hexa CDF pg <3.8 3.8 30 0.100 0.380 N/A 

2,3,4,6,7,8-Hexa CDF pg <4.8 4.8 30 0.100 0.480 N/A 

1,2,3,7,8,9-Hexa CDF pg <5.3 5.3 30 0.100 0.530 N/A 

1,2,3,4,6,7,8-Hepta CDF pg <2.9 2.9 30 0.0100 0.0290 N/A 

1 ,2,3,4, 7 ,8,9-Hepta CDF pg <4.0 4.0 30 0.0100 0.0400 N/A 

1 ,2,3,4,6, 7 ,8,9-0cta CDF pg <5.2 5.2 300 0.000300 0.00156 N/A 

Total Tetra CDF pg <2.5 2.5 30 N/A N/A N/A 

Total Penta CDF pg <7.4 7.4 30 N/A N/A N/A 

Total Hexa CDF pg <4.4 4.4 30 N/A N/A N/A 

Total Hepta CDF pg <3.4 3.4 30 N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chloro Dibenzo-p-Dioxin, •• CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEO = Toxic Equivalency Quotient, 

QC Batch 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency F;;ctors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 9 of29 

Ma:<xam Analytics lrnernational corporation o/a Maxxam Analytlcs 6740 CampoDeQo Road, MJsslssauga. Ontario, L5N as Tel: (905) 817-5700 Toll-Free: aoo-563·6266 Fax: (905) 817-5777 wwwmaxxam.ca 
M azS}la m 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

Sampling Date 

COG Number 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1495 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units TRAIN EDL RDL TEF (2005 WHO) rEQ(DL) somers 

BLANK·M23/PCB 

TOTAL TOXIC EQUIVALENCY pg N/A N/A N/A N/A 17.5 N/A 

Surrogate Recovery (%) 

C13-1234678 HeptaCDD * % 125 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDF ** % 130 N/A N/A N/A N/A N/A 

C13-123478 HexaCDD % 93 N/A N/A N/A N/A N/A 

C13-123478 HexaCDF % 101 N/A N/A N/A N/A N/A 

C13-1234789 HeptaCDF % 85 N/A N/A N/A N/A N/A 

C13-123678 HexaCDD % 76 N/A N/A N/A N/A N/A 

C13-123678 HexaCDF % 73 N/A N/A N/A N/A N/A 

C13-12378 PentaCDD % 44 N/A N/A N/A N/A N/A 

C13-12378 PentaCDF % 49 N/A N/A N/A N/A N/A 

C13-123789 HexaCDF % 73 N/A N/A N/A N/A N/A 

C13-23478 PentaCDF % 99 N/A N/A N/A N/A N/A 

C13-2378 TetraCDD % 60 N/A N/A N/A N/A N/A 

C13-2378 TetraCDF % 88 N/A N/A N/A N/A N/A 

C 13-0ctachlorodibenzo-p-Dioxin % 120 N/A N/A N/A N/A N/A 

Cl37-2378 TetraCDD % 129 N/A N/A N/A N/A N/A 

N/ A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chiaro Dibenzo-p-Dioxin, ** CDF = Chiaro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEO = Toxic Equivalency Quotient, 

QC Batch 

N/A 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 10 of 29 

Ma<Xam Analytics lrnernational COrporation o/a Maxxam Anal~'tics 6740 campobello Road. Mlssissauga. Ontario. L5N 2L8 Tel: (905) 817-5700 Toll-Free: SOD-563-6266 Fax: {905) 817-5777 www.maxxam.ca 
1\/la&arn 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

!Sampling Date 

COC Number 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. -FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1497 

2013/03/19 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) TEQ(DL) somers 

1·BH2-M23/PCB 

2,3,7,8-Tetra COD* pg <3.3 3.3 30 1.00 3.30 N/A 

1,2,3,7,8-Penta COD pg <3.5 3.5 30 1.00 3.50 N/A 

1 ,2,3,4,7,8-Hexa COD pg <4.9 4.9 30 0.100 0.490 N/A 

1 ,2,3,6,7,8-Hexa COD pg <4.8 4.8 30 0.100 0.480 N/A 

1,2,3,7,8,9-Hexa COD pg <4.8 4.8 30 0.100 0.480 N/A 

1,2,3,4,6,7,8-Hepta COD pg 15.8 5.8 30 0.0100 0.158 N/A 

1,2,3,4,6,7,8,9-0cta COD pg 30.4 5.3 300 0.000300 0.00912 N/A 

Total Tetra COD pg 123 3.3 30 N/A N/A N/A 

Total Penta COD pg 8.0 3.5 30 N/A N/A N/A 

Total Hexa COD pg 21.2 4.9 30 N/A N/A N/A 

Total Hepta COD pg 36.6 5.8 30 N/A N/A N/A 

2,3,7,8-Tetra CDF ** pg <190 (1) 190 30 0.100 19.0 N/A 

1 ,2,3, 7 ,8-Penta CDF pg 21.2 4.6 30 0.0300 0.636 N/A 

2,3,4,7,8-Penta CDF pg 23.4 (2) 4.4 30 0.300 7.02 N/A 

1,2,3,4,7,8-Hexa CDF pg 33.3 3.2 30 0.100 3.33 N/A 

1,2,3,6,7,8-Hexa CDF pg 15.1 3.1 30 0.100 1.51 N/A 

2,3,4,6,7,8-Hexa CDF pg 12.2 3.9 30 0.100 1.22 N/A 

1,2,3,7,8,9-Hexa CDF pg <4.4 4.4 30 0.100 0.440 N/A 

1,2,3,4,6,7,8-Hepta CDF pg 25.7 3.4 30 0.0100 0.257 N/A 

1,2,3,4,7,8,9-Hepta CDF pg <4.6 4.6 30 0.0100 0.0460 N/A 

1,2,3,4,6,7,8,9-0cta CDF pg 16.1 (2) 5.2 300 0.000300 0.00483 N/A 

Total Tetra CDF pg 1210 5.3 30 N/A N/A N/A 

Total Penta CDF pg 329 4.5 30 N/A N/A N/A 

Total Hexa CDF pg 124 3.6 30 N/A N/A N/A 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF =Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

pc Batch 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

!wH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) RT > 3 seconds- PCDD/DF analysis- Peak detected exceeds expected retention time (from internal standard) by 

greater than 3 seconds. 

( 2) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 11 of29 

Ma'xam Analylics lrnernalional COrporatiOn o/a Ma""am Analy1ics 6740 CampobeRo Road, MISSISsauga, Ontario, L51\1 21.8 Tel: (905) 817-5700 TOII·Free: 800.563·6266 Fax: (905) 817·5777 www.maxxam.ca 
Ma'§am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

Sampling Date 

OC Number 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1497 

2013/03/19 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) fEQ(DL) somers 

1-BH2-M23/PCB 

Total Hepta CDF ** pg 34.9 3.9 30 N/A N/A N/A 

Confirmation 2,3,7,8-Tetra CDF pg 39.8 3.2 30 0.100 3.98 N/A 

TOTAL TOXIC EQUIVALENCY pg N/A N/A N/A N/A 26.9 N/A 

Surrogate Recovery (%} 

Confirmation C13-2378 TetraCDF % 78 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDD * % 112 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDF % 115 N/A N/A N/A N/A N/A 

C13-123478 HexaCDD % 93 N/A N/A N/A N/A N/A 

C13-123478 HexaCDF % 103 N/A N/A N/A N/A N/A 

C13-1234789 HeptaCDF % 91 N/A N/A N/A N/A N/A 

C13-123678 HexaCDD % 80 N/A N/A N/A N/A N/A 

C13-123678 HexaCDF % 79 N/A N/A N/A N/A N/A 

C13-12378 PentaCDD % 77 N/A N/A N/A N/A N/A 

C13-12378 PentaCDF % 86 N/A N/A N/A N/A N/A 

C13-123789 HexaCDF % 77 N/A N/A N/A N/A N/A 

C13-23478 PentaCDF % 97 N/A N/A N/A N/A N/A 

C13-2378 TetraCDD % 66 N/A N/A N/A N/A N/A 

C13-2378 TetraCDF % 90 N/A N/A N/A N/A N/A 

C13-0ctachlorodibenzo-p-Dioxin % 112 N/A N/A N/A N/A N/A 

Cl37-2378 TetraCDD % 127 N/A N/A N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

• COD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

QC Batch 

3190066 

3191218 

N/A 

3191218 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 12 of 29 

1\!la'Xam Analylocs lrnernational COrporation o/a Maxxarn Anal~'lics 6740 C<mpobello Road, MlssiSS8!JIIll, Ontario, L5N 2LB Tel: (905) 817-5700 TOll-Free: BOo-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
1\./1 a ({)2 a m 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

Sampling Date 

OC Number 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1498 

2013/03/19 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) fEQ(DL) somers 

2-BH2-M23/PCB 

2,3,7,8-Tetra CDD * pg <3.7 3.7 30 1.00 3.70 N/A 

1 ,2,3, 7 ,8-Penta CDD pg <3.6 3.6 30 1.00 3.60 N/A 

1 ,2,3,4,7,8-Hexa CDD pg <3.6 3.6 30 0.100 0.360 N/A 

1 ,2,3,6,7,8-Hexa CDD pg <3.4 3.4 30 0.100 0.340 N/A 

1 ,2,3, 7 ,8,9-Hexa CDD pg <3.5 3.5 30 0.100 0.350 N/A 

1 ,2,3,4,6,7,8-Hepta CDD pg <3.5 3.5 30 0.0100 0.0350 N/A 

1 ,2,3,4,6, 7,8,9-0cta CDD pg 12.3 4.1 300 0.000300 0.00369 N/A 

Total Tetra CDD pg 16.1 3.7 30 N/A N/A N/A 

Total Penta CDD pg <4.0 (1) 4.0 30 N/A N/A N/A 

Total Hexa CDD pg <9.6 (1) 9.6 30 N/A N/A N/A 

Total Hepta CDD pg <3.5 3.5 30 N/A N/A N/A 

2,3,7,8-Tetra CDF ** pg <53~ 53 30 0.100 5.30 N/A 

1 ,2,3, 7 ,8-Penta CDF pg 5.9 3.5 30 0.0300 0.177 N/A 

2,3,4,7,8-Penta CDF pg 6.0 3.3 30 0.300 1.80 N/A 

1 ,2,3,4,7,8-Hexa CDF pg 8.0 3.4 30 0.100 0.800 N/A 

1 ,2,3,6, 7 ,8-Hexa CDF pg <3.2 3.2 30 0.100 0.320 N/A 

2,3,4,6,7,8-Hexa CDF pg <4.1 4.1 30 0.100 0.410 N/A 

1 ,2,3, 7 ,8,9-Hexa CDF pg <4.5 4.5 30 0.100 0.450 N/A 

1,2,3,4,6,7,8-Hepta CDF pg 5.9@) 2.3 30 0.0100 0.0590 N/A 

1 ,2,3,4, 7 ,8,9-Hepta CDF pg <3.1 3.1 30 0.0100 0.0310 N/A 

1 ,2,3,4,6, 7,8,9-0cta CDF pg <5.3 5.3 300 0.000300 0.00159 N/A 

Total Tetra CDF pg 335 4.5 30 N/A N/A N/A 

Total Penta CDF pg 67.8 3.4 30 N/A N/A N/A 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* CDD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

QC Batch 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organizaticr., Human and Mammalian Toxic Equiva!ency Factors for Dioxins &.:c 

Dioxin-like Compounds 

( 1 ) EMPC I NDR - Peak detected does net rr:eet ratio criteria and has resulted in an elevated detection limit. 

( 2) RT > 3 seconds- PCDD/DF analysis- Peak detected exceeds expected retention time (from internal standard) by 

greater than 3 seconds. 

( 3) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 13 of 29 

Mauam Analylics Jrnernational Corporation o!a Maxxam Analytics 6740 campobello Road, MlssissaJga, Onlario, L5N 2LB Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma?§2am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

Sampling Date 

COC Number 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1498 

2013/03/19 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) ~EQ(DL) somers 

2-BH2-M23/PCB 

Total Hexa CDF ** pg 18.3 3.7 30 N/A N/A N/A 

Total Hepta CDF pg 5.9 (1) 2.6 30 N/A N/A N/A 

Confirmation 2,3,7,8-Tetra CDF pg 10.1 3.4 30 0.100 1.01 N/A 

TOTAL TOXIC EQUIVALENCY pg N/A N/A N/A N/A 13.4 N/A 

Surrogate Recovery(%) 

Confirmation C13-2378 TetraCDF 'Yo 76 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDD * 'Yo 119 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDF 'Yo 111 N/A N/A N/A N/A N/A 

C13-123478 HexaCDD 'Yo 106 N/A N/A N/A N/A N/A 

C13-123478 HexaCDF 'Yo 107 N/A N/A N/A N/A N/A 

C13-1234789 HeptaCDF 'Yo 89 N/A N/A N/A N/A N/A 

C13-123678 HexaCDD 'Yo 73 N/A N/A N/A N/A N/A 

C13-123678 HexaCDF 'Yo 77 N/A N/A N/A N/A N/A 

C13-12378 PentaCDD o/o 88 N/A N/A N/A N/A N/A 

C13-12378 PentaCDF 'Yo 93 N/A N/A N/A N/A N/A 

C13-123789 HexaCDF 'Yo 75 N/A N/A N/A N/A N/A 

C13-23478 PentaCDF 'Yo 99 N/A N/A N/A N/A N/A 

C13-2378 TetraCDD 'Yo 65 N/A N/A N/A N/A N/A 

C13-2378 TetraCDF 'Yo 85 N/A N/A N/A N/A N/A 

C13-0ctachlorodibenzo-p-Dioxin 'Yo 105 N/A N/A N/A N/A N/A 

Cl37-2378 TetraCDD 'Yo 129 N/A N/A N/A N/A N/A 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chloro Dibenzo-p-Dioxin, ** CDF = Chiaro Dibenzo-p-Furan 

TEF =Toxic Equivalency Factor, TEQ =Toxic Equivalency Quotient, 

QC Batch 

3190066 

3190066 

3191218 

N/A 

3191218 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Marnm&:'an Toxic Equiv&i~· :•1 Factors for [.,cxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 14 of 29 

' 

I 

1\ilaxxam Analytics International COrporation ola Maxxam AnalytiGs 6740 GampobeHo Road, Mlssissauga. Ontario, LSN 2L8 Tel: (905) 817-5700 Toll-Free: 800-563·6266 Fax: (905) 817·5777 wvvw.mal<xam.oa 
Ma({)2am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

~ampling Date 

COG Number 

Keika Ventures 

Client Project #: Tl1550 

Site location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1499 

2013103119 

00:01 

NIA TOXIC EQUIVALENCY #of 

Units RUN IEDL RDL TEF (2005 WHO) fEQ(DL) somers 

3-BH2-M23/PCB 

2,3,7,8-Tetra COD* pg <4.1 4.1 30 1.00 4.10 NIA 

1,2,3,7,8-Penta COD pg <4.1 4.1 30 1.00 4.10 NIA 

1,2,3,4,7,8-Hexa COD pg <3.9 3.9 30 0.100 0.390 NIA 

1 ,2,3,6,7,8-Hexa COD pg <3.8 3.8 30 0.100 0.380 NIA 

1 ,2,3, 7 ,8,9-Hexa COD pg <3.8 3.8 30 0.100 0.380 NIA 

1,2,3,4,6,7,8-Hepta COD pg <3.2 3.2 30 0.0100 0.0320 NIA 

1,2,3,4,6,7,8,9-0cta COD pg 7.7 3.3 300 0.000300 0.00231 N/A 

Total Tetra COD pg 24.8 4.1 30 NIA N/A N/A 

Total Penta COD pg 4.9 4.1 30 NIA N/A N/A 

Total Hexa COD pg <9.8 (1) 9.8 30 N/A NIA N/A 

Total Hepta COD pg <3.2 3.2 30 NIA NIA N/A 

2,3,7,8-Tetra CDF ** pg <78 (2) 78 30 0.100 7.80 N/A 

1 ,2,3,7,8-Penta CDF pg 9.7 4.4 30 0.0300 0.291 N/A 

2,3,4,7,8-Penta CDF pg 12.6 4.2 30 0.300 3.78 N/A 

1 ,2,3,4,7,8-Hexa CDF pg <13@) 13 30 0.100 1.30 N/A 

1 ,2,3,6,7,8-Hexa CDF pg <5.2@) 5.2 30 0.100 0.520 NIA 

2,3,4,6,7,8-Hexa CDF pg <4.1 4.1 30 0.100 0.410 N/A 

1,2,3,7,8,9-Hexa CDF pg <4.5 4.5 30 0.100 0.450 N/A 

1 ,2,3,4,6, 7,8-Hepta CDF pg 7.2 (4) 2.9 30 0.0100 0.0720 N/A 

1 ,2,3,4,7,8,9-Hepta CDF pg <4.0 4.0 30 0.0100 0.0400 N/A 

1 ,2,3,4,6,7 ,8,9-0cta CDF pg 5.3 3.6 300 0.000300 0.00159 N/A 

Total Tetra CDF pg 455 2.9 30 N/A NIA N/A 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

pc Batch 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I NOR - Peak detected does not meet ratio criteria and has resulted in an elevated detection limit. 

( 2) RT > 3 seconds - PCDD/DF analysis - Peak detected exceeds expected retention time (from internal standard) by 

greater than 3 seconds. 

( 3) EMPC I OPE - Diphenylether interierence present caused dibenzofuran detected to become a "non-detect" with an 

elevated detection limit. 

( 4) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 15 of 29 

Ma'Xam Analytics lrnerna1i<lnal COrporation 0/a Maxxarn Anal~'1ics 6740 C;mpobello Roa<l, Mlsslssauga, Ontario, L5N 21..8 Tel: (905) 817-5700 Toii-Ftee: BOQ-563-6266 Fax: {905) 817-5777 www.maxxarn.ca 
J\/ie:l"§am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

Sampling Date 

COC Number 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1499 

2013/03/19 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) ITEQ(DL) somers 

3-BH2-M23/PCB 

Total Penta CDF ** pg 126 4.3 30 N/A N/A N/A 

Total Hexa CDF pg 15.6 3.7 30 N/A N/A N/A 

Total Hepta CDF pg 7.2 (1) 3.4 30 N/A N/A N/A 

Confirmation 2,3,7,8-Tetra CDF pg 15.0 3.0 30 0.100 1.50 N/A 

TOTAL TOXIC EQUIVALENCY pg N/A N/A N/A N/A 17.7 N/A 

Surrogate Recovery (%) 

Confirmation C13-2378 TetraCDF % 71 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDD * % 97 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDF % 101 N/A N/A N/A N/A N/A 

C13-123478 HexaCDD % 99 N/A N/A N/A N/A N/A 

C13-123478 HexaCDF % 96 N/A N/A N/A N/A N/A 

C13-1234789 HeptaCDF % 93 N/A N/A N/A N/A N/A 

C13-123678 HexaCDD % 73 N/A N/A N/A N/A N/A 

C13-123678 HexaCDF % 81 N/A N/A N/A N/A N/A 

C13-12378 PentaCDD % 84 N/A N/A N/A N/A N/A 

C13-12378 PentaCDF % 83 N/A N/A N/A N/A N/A 

C13-123789 HexaCDF % 76 N/A N/A N/A N/A N/A 

C13-23478 PentaCDF % 105 N/A N/A N/A N/A N/A 

C13-2378 TetraCDD % 57 N/A N/A N/A N/A N/A 

C13-2378 TetraCDF % 77 N/A N/A N/A N/A N/A 

C 13-0ctachlorodibenzo-p-Dioxin % 98 N/A N/A N/A N/A N/A 

Cl37-2378 TetraCDD % 124 N/A N/A N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chiaro Dibenzo-p-Dioxin, ** CDF = Chiaro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEO = Toxic Equivalency Quotient, 

QC Batch 

3190066 

3190066 

3190066 

3191218 

N/A 

3191218 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

lfhe Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 16 of 29 

1\/ia<Xam Analytlcs ltnernatlonal COrporatiOn o/a Maxxam Analytlcs 6740 C<mpobeiiO Aoa!l, MIS&ISsauga. Ontario, L5N :21.6 Tel: (905) 817·6700 Toll.f'ree: SfJ0-563-6266 fax: (905) 817-5777 www.ma.xam.ca 
Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam 10 

Sampling Date 

r.oc Number 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1500 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) ~EQ(DL) somers 

1·BH5-M23/PCB 

2,3,7,8-Tetra COD* pg 6.7 (1} 3.5 30 1.00 6.70 N/A 

1,2,3,7,8-Penta COD pg 3.5 2.8 30 1.00 3.50 N/A 

1,2,3,4,7,8-Hexa COD pg <3.2 3.2 30 0.100 0.320 N/A 

1 ,2,3,6, 7 ,8-Hexa COD pg <3.1 3.1 30 0.100 0.310 N/A 

1,2,3,7,8,9-Hexa COD pg <3.2 3.2 30 0.100 0.320 N/A 

1 ,2,3,4,6, 7,8-Hepta COD pg 5.2 (1} 3.4 30 0.0100 0.0520 N/A 

1,2,3,4,6,7,8,9-0cta COD pg 11.9 (1} 3.1 300 0.000300 0.00357 N/A 

!Total Tetra COD pg 121 3.5 30 N/A N/A N/A 

Total Penta COD pg 31.8 2.8 30 N/A N/A N/A 

Total Hexa COD pg 11.8 3.2 30 N/A N/A N/A 

Total Hepta COD pg 10.8 3.4 30 N/A N/A N/A 

2,3,7,8-Tetra CDF ** pg 220 3.1 30 0.100 22.0 N/A 

1,2,3,7,8-Penta CDF pg 23.7 3.6 30 0.0300 0.711 N/A 

2,3,4,7,8-Penta CDF pg 20.6 3.5 30 0.300 6.18 N/A 

1 ,2,3,4,7,8-Hexa CDF pg 13.0 2.8 30 0.100 1.30 N/A 

1 ,2,3,6, 7 ,8-Hexa CDF pg 5.5 2.7 30 0.100 0.550 N/A 

2,3,4,6,7,8-Hexa CDF pg <3.4 3.4 30 0.100 0.340 N/A 

1 ,2,3, 7 ,8,9-Hexa CDF pg <3.8 3.8 30 0.100 0.380 N/A 

1 ,2,3,4,6,7,8-Hepta CDF pg 4.6 (1} 2.6 30 0.0100 0.0460 N/A 

1 ,2,3,4, 7 ,8,9-Hepta CDF pg <3.5 3.5 30 0.0100 0.0350 N/A 

1,2,3,4,6,7,8,9-0cta CDF pg 4.5 (1} 3.5 300 0.000300 0.00135 N/A 

jTotal Tetra CDF pg 1560 3.1 30 N/A N/A N/A 

Total Penta CDF pg 396 3.6 30 N/A N/A N/A 

Total Hexa CDF pg 46.1 3.1 30 N/A N/A N/A 

Total Hepta CDF pg 4.6 (1} 3.0 30 N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEO = Toxic Equivalency Quotient, 

~c Batch 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEO} value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 17 of 29 

1\/laxxam Analytics International COrporation o/a Maxxam Analytios 6740 C<impobaRo Road, Mlsslssauga, Ontario, L5N 21..8 Tel: (905) 817·5700 Toll-free: SOD-563·6266 Fax: (905) 817·5777 www.maxxam.ca 
Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam 10 

~ampling Date 

~oc Number 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC.- FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1500 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF {2005 WHO) ITEQ{DL) somers 

1-BH5-M23/PCB 

Confirmation 2,3,7,8-Tetra CDF •• pg 54.4 3.2 30 0.100 5.44 N/A 

TOTAL TOXIC EQUIVALENCY pg N/A N/A N/A N/A 26.2 N/A 

Surrogate Recovery (%) 

Confirmation C13-2378 TetraCDF % 65 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDD • % 96 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDF % 107 N/A N/A N/A N/A N/A 

C13-123478 HexaCDD % 106 N/A N/A N/A N/A N/A 

C13-123478 HexaCDF % 104 N/A N/A N/A N/A N/A 

C13-1234789 HeptaCDF % 89 N/A N/A N/A N/A N/A 

C13-123678 HexaCDD % 91 N/A N/A N/A N/A N/A 

C13-123678 HexaCDF % 89 N/A N/A N/A N/A N/A 

C13-12378 PentaCDD % 88 N/A N/A N/A N/A N/A 

C13-12378 PentaCDF % 84 N/A N/A N/A N/A N/A 

C13-123789 HexaCDF % 80 N/A N/A N/A N/A N/A 

C13-23478 PentaCDF % 114 N/A N/A N/A N/A N/A 

C13-2378 TetraCDD % 58 N/A N/A N/A N/A N/A 

C13-2378 TetraCDF % 71 N/A N/A N/A N/A N/A 

C 13-0ctachlorodibenzo-p-Dioxin % 108 N/A N/A N/A N/A N/A 

Cl37-2378 TetraCDD % 127 N/A N/A N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

• COD = Chiaro Dibenzo-p-Dioxin, .. CDF = Chiaro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

QC Batch 

3191218 

N/A 

3191218 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

!The Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 18 of 29 

Ma<Xam Analylics lrnernatiOnal COrporatiOn o/a Maxxam Anal~'lics 6740 campobello Road, Mlsslssauga, OntariO, L5N 21..8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

Sampling Date 

OC Number 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS {STACK SAMPLING TRAIN) 

RC1505 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) ~EQ(DL) somers 

2·BH5·M23/PCB 

2,3,7,8-Tetra COD* pg 11.9 (1) 4.1 30 1.00 11.9 N/A 

1,2,3,7,8-Penta COD pg 7.8 (1) 3.6 30 1.00 7.80 N/A 

1,2,3,4,7,8-Hexa COD pg 4.5 3.2 30 0.100 0.450 N/A 

1,2,3,6,7,8-Hexa COD pg 5.6 3.1 30 0.100 0.560 N/A 

1 ,2,3,7,8,9-Hexa COD pg 6.0 3.2 30 0.100 0.600 N/A 

1,2,3,4,6,7,8-Hepta COD pg 13.7 2.6 30 0.0100 0.137 N/A 

1 ,2,3,4,6, 7,8,9-0cta COD pg 37.8 5.4 300 0.000300 0.0113 N/A 

Total Tetra COD pg 194 4.1 30 N/A N/A N/A 

Total Penta COD pg 79.7 3.6 30 N/A N/A N/A 

Total Hexa COD pg 27.4 3.2 30 N/A N/A N/A 

Total Hepta COD pg 25.1 2.6 30 N/A N/A N/A 

2,3,7,8-Tetra CDF ** pg <260 (2) 260 30 0.100 26.0 NIA 

1,2,3,7,8-Penta CDF pg 32.9 4.9 30 0.0300 0.987 N/A 

2,3,4,7,8-Penta CDF pg 28.7 4.6 30 0.300 8.61 N/A 

1,2,3,4,7,8-Hexa CDF pg 20.2 (3) 3.6 30 0.100 2.02 NIA 

1,2,3,6,7,8-Hexa CDF pg 11.3 (1) 3.4 30 0.100 1.13 NIA 

2,3,4,6,7,8-Hexa CDF pg 8.4 4.3 30 0.100 0.840 NIA 

1 ,2,3,7,8,9-Hexa CDF pg <4.8 4.8 30 0.100 0.480 NIA 

1,2,3,4,6,7,8-Hepta CDF pg 10.9 (1) 2.6 30 0.0100 0.109 N/A 

1 ,2,3,4,7,8,9-Hepta CDF pg <3.6 3.6 30 0.0100 0.0360 N/A 

1,2,3,4,6,7,8,9-0cta CDF pg 17.5 3.5 300 0.000300 0.00525 N/A 

Total Tetra CDF pg 1830 3.5 30 N/A N/A N/A 

Total Penta CDF pg 465 4.8 30 N/A N/A N/A 

Nl A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

• COD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF =Toxic Equivalency Factor, TEO= Toxic Equivalency Quotient, 

QC Batch 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

( 2) RT > 3 seconds- PCDDIDF analysis- Peak detected exceeds expected retention time (from internal standara) 'Jy 

greater than 3 seconds. 

( 3) EMPC I Merged Peak 

Page 19 of 29 

i 

1\!la'Xam Analytics lrrternational corporation o/a Maxxam Anal~"tics 6740 canpoballo Road, Mlsslssauga, Onlario, L5N 2L8 Tel: (905) 817·5700 Toii·Free: 800.563·6266 Fax: (905) 817·5777 www.maxxam.ca 
Ma1))i.arn 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam 10 

Sampling Date 

toe Number 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1505 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN fi=DL RDL TEF (2005 WHO) rreQ{DL) somers 

2-BH5-M23/PCB 

Total Hexa CDF •• pg 77.5 4.0 30 N/A N/A N/A 

Total Hepta CDF pg 10.9 (1) 3.0 30 N/A N/A N/A 

Confirmation 2,3,7,8-Tetra CDF pg 68.7 6.5 30 0.100 6.87 N/A 

TOTAL TOXIC EQUIVALENCY pg N/A N/A N/A N/A 42.5 N/A 

Surrogate Recovery(%) 

Confirmation C13-2378 TetraCDF % 53 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDD * % 99 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDF % 100 N/A N/A N/A N/A N/A 

C13-123478 HexaCDD % 104 N/A N/A N/A N/A N/A 

C13-123478 HexaCDF % 105 N/A N/A N/A N/A N/A 

C13-1234789 HeptaCDF % 88 N/A N/A N/A N/A N/A 

C13-123678 HexaCDD % 79 N/A N/A N/A N/A N/A 

C13-123678 HexaCDF % 77 N/A N/A N/A N/A N/A 

C13-12378 PentaCDD % 75 N/A N/A N/A N/A N/A 

C13-12378 PentaCDF % 66 N/A N/A N/A N/A N/A 

C13-123789 HexaCDF % 73 N/A N/A N/A N/A N/A 

C13-23478 PentaCDF % 134 (2) N/A N/A N/A N/A N/A 

C13-2378 TetraCDD % 49 N/A N/A N/A N/A N/A 

C13-2378 TetraCDF % 53 N/A N/A N/A N/A N/A 

C 13-0ctachlorodibenzo-p-Dioxin % 98 N/A N/A N/A N/A N/A 

Cl37-2378 TetraCDD % 165 (2) N/A N/A N/A N/A N/A 

N/ A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chiaro Dibenzo-p-Dioxin, ** CDF = Chiaro Dibenzo-p-Furan 

TEF =Toxic Equivalency Factor, TEO= Toxic Equivalency Quotient, 

~c Batch 

3190066 

3190066 

3191218 

N/A 

3191218 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEO) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

( 2) Field spike exceeds upper control limit (70-130%) 

Page20of29 

Ma:<xam AnalyliGs lrnernationat COrporation o/a Maxxam Anal}"tics 6740 C<mpobello Road, Mlssissauga, Onlario,l5N 2LB Tel: (905) 817-5700 Toll-free: BD0-563-6266 Fax: (905) 817-5777 wwwmaxxam.ca 
Ma~am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam 10 

Sampling Date 

OC Number 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1511 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) rrEQ(DL) somers QC Batch 

3-BH5-M23/PCB 

2,3,7,8-Tetra COD* pg 9.5 (1) 3.5 30 1.00 9.50 N/A 3190066 

1,2,3,7,8-Penta COD pg 6.6 3.4 30 1.00 6.60 N/A 3190066 

1,2,3,4,7,8-Hexa COD pg <3.3 3.3 30 0.100 0.330 N/A 3190066 

1 ,2,3,6, 7 ,8-Hexa COD pg <3.2 3.2 30 0.100 0.320 N/A 3190066 

1,2,3,7,8,9-Hexa COD pg 4.6 3.2 30 0.100 0.460 N/A 3190066 

1 ,2,3,4,6,7,8-Hepta COD pg 5.9 (1) 3.1 30 0.0100 0.0590 N/A 3190066 

1,2,3,4,6,7,8,9-0cta COD pg 26.5 (1) 4.7 300 0.000300 0.00795 N/A 3190066 

Total Tetra COD pg 326 3.5 30 N/A N/A N/A 3190066 

Total Penta COD pg 105 3.4 30 N/A N/A N/A 3190066 

Total Hexa COD pg 4.6 3.3 30 N/A N/A N/A 3190066 

Total Hepta COD pg 5.9 (1) 3.1 30 N/A N/A N/A 3190066 

2,3,7,8-Tetra CDF •• pg <460 (2) 460 30 0.100 46.0 N/A 3190066 

1,2,3,7,8-Penta CDF pg 46.3 3.8 30 0.0300 1.39 N/A 3190066 

2,3,4, 7 ,8-Penta CDF pg 38.1 3.6 30 0.300 11.4 N/A 3190066 

1,2,3,4,7,8-Hexa CDF pg 26.8 2.5 30 0.100 2.68 N/A 3190066 

1,2,3,6,7,8-Hexa CDF pg 13.4 2.3 30 0.100 1.34 N/A 3190066 

2,3,4,6,7,8-Hexa CDF pg 5.1 3.0 30 0.100 0.510 N/A 3190066 

1,2,3,7,8,9-Hexa CDF pg <3.3 3.3 30 0.100 0.330 N/A 3190066 

1 ,2,3,4,6,7,8-Hepta CDF pg 10.1 (1) 3.7 30 0.0100 0.101 N/A 3190066 

1,2,3,4,7,8,9-Hepta CDF pg <5.0 5.0 30 0.0100 0.0500 N/A 3190066 

1 ,2,3,4,6, 7 ,8,9-0cta CDF pg 33.6 5.2 300 0.000300 0.0101 N/A 3190066 

Total Tetra CDF pg 3230 4.0 30 N/A N/A N/A 3190066 

Total Penta CDF pg 757 3.7 30 N/A N/A N/A 3190066 

Total Hexa CDF pg 118 2.7 30 N/A N/A N/A 3190066 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

• COD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

( 2) RT > 3 seconds - PCDD/DF analysis - Peak detected exceed:; expected retention time (from ir.tu'lal s:.:c ;<;ard) by 

greater than 3 seconds. 

Page 21 of29 

I 

I 

1\ilaxxam Analy!ics ltnernational Corporation o!a Maxxam Analytics 6740 Canpobello Road, Mlssissauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: SOQ-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma-62am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

Sampling Date 

COC Number 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

DIOXINS AND FURANS BY HRMS (STACK SAMPLING TRAIN) 

RC1511 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) ~EQ(DL) somers 

3-BH5-M23/PCB 

Total Hepta CDF •• pg 16.3 4.2 30 N/A N/A N/A 

Confirmation 2,3,7,8-Tetra CDF pg 96.0 3.4 30 0.100 9.60 N/A 

TOTAL TOXIC EQUIVALENCY pg N/A N/A N/A N/A 44.7 N/A 

Surrogate Recovery (%) 

Confirmation C13-2378 TetraCDF % 71 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDD * % 104 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDF % 118 N/A N/A N/A N/A N/A 

C13-123478 HexaCDD % 109 N/A N/A N/A N/A N/A 

C13-123478 HexaCDF % 104 N/A N/A N/A N/A N/A 

C13-1234789 HeptaCDF % 85 N/A N/A N/A N/A N/A 

C13-123678 HexaCDD % 79 N/A N/A N/A N/A N/A 

C13-123678 HexaCDF % 85 N/A N/A N/A N/A N/A 

C13-12378 PentaCDD % 81 N/A N/A N/A N/A N/A 

C13-12378 PentaCDF % 86 NIA N/A N/A N/A N/A 

C13-123789 HexaCDF % 82 N/A N/A N/A N/A N/A 

C13-23478 PentaCDF % 98 N/A N/A N/A N/A N/A 

C13-2378 TetraCDD % 59 N/A N/A N/A N/A N/A 

C13-2378 TetraCDF % 76 N/A N/A N/A N/A N/A 

C13-0ctachlorodibenzo-p-Dioxin % 95 N/A N/A N/A N/A N/A 

Cl37-2378 TetraCDD % 125 N/A N/A N/A N/A N/A 

N/A = Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

* COD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

pc Batch 

3190066 

3191218 

N/A 

3191218 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

3190066 

The Total Toxic Equivalency (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

~H0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 22 of29 

Ma.<xam Analy!ics lrnernational COrporation o/a Maxxam Analytics 6740 Gampobello Road, MlssiSsauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma({)2.am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID RC1495 

Sample ID TRAIN BLANK-M23/PCB 

Matrix Stack Sampling Train 

Maxxam ID RC1497 

Sample ID RUN 1-BH2-M23/PCB 

Matrix Stack Sampling Train 

Test Description 

2 3 7 8-TCDF Confirmation (M23) 

Dioxins/Furans in Air (Method 23) 

PCB Congeners in Air(1668A) 

Test 

Maxxam ID RC1498 

Sample ID RUN 2-BH2-M23/PCB 

Matrix Stack Sampling Train 

D escr1pt1on 

2 3 7 8-TCDF Confirmation (M23) 

Dioxins/Furans in Air (Method 23) 

PCB Congeners in Air (1668A) 

Maxxam ID RC1499 

Sample ID RUN 3-BH2-M23/PCB 

Matrix Stack Sampling Train 

Test Description 

2 3 7 8-TCDF Confirmation (M23) 

Dioxins/Furans in Air (Method 23) 

PCB Congeners in Air (1668A) 

Maxxam ID RC1500 

Sample ID RUN 1-BH5-M23/PCB 

Matrix Stack Sampling Train 

Test Description 

2 3 7 8-TCDF Confirmation (M23) 

Dioxins/Furans in Air (Method 23) 

PCB Congeners in Air (1668A) 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

Test Summary 

Instrumentation Batch Extracted 

HRMS/MS 3190066 2013/04/16 

HRMS/MSEC 3182506 2013/04/16 

Instrumentation Batch Extracted 

HRMS/MS 3191218 N/A 

HRMS/MS 3190066 2013/04/16 

HRMS/MSEC 3182506 2013/04/16 

I ns t t rumen a r 1on B ac t h E X tract e d 

HRMS/MS 3191218 N/A 

HRMS/MS 3190066 2013/04/16 

HRMS/MSEC 3182506 2013/04/16 

Instrumentation B h ate E xtracte d 

HRMS/MS 3191218 N/A 

HRMS/MS 3190066 2013/04/16 

HRMS/MSEC 3182506 2013/04/16 

Instrumentation Batch Extracted 

HRMS/MS 3191218 N/A 

HRMS/MS 3190066 2013/04/16 

HRMS/MSEC 3182506 2013/04/16 

Page23 of29 

Analyzed 

2013/04/24 

2013/04/25 

2013/04/24 

A na1yze I d 

2013/04/24 

2013/04/25 

2013/04/24 

A na1yze I d 

2013/04/24 

2013/04/25 

2013/04/24 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Collected 2013/03/19 

Shipped 

Received 2013/04/06 

Analyst 

Vica Cioranic 

OwenCosbv 

Cathv Xu 

Collected 2013/03/19 

Shipped 

Received 2013/04/06 

A na1ys I t 

Vica Cioranic 

Owen Cosby 

Cathy Xu 

Collected 2013/03/19 

Shipped 

Received 2013/04/06 

A na1yst I 

Vica Cioranic 

Owen Cosby 

Cathy Xu 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

A na1vze I d A nalyst I 

2013/04/24 Vica Cioranic 

2013/04/25 OwenCosbv 

2013/04/24 Cathv Xu 

Ma<xam Analytics lrtternational COrporation o/a Maxxam Analytics 6740 campobello Roall, MISSiSSauga, Ontario, L5N 2L8 Tel: (905i 817-5700 Toll-Free: SOQ-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
1\/f a (!52. am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID RC1505 

Sample ID RUN 2-BH5-M23/PCB 

Matrix Stack Sampling Train 

Test Description 

2 3 7 8-TCDF Confirmation (M23) 

Dioxins/Furans in Air (Method 23) 

PCB Conqeners in Air (1668A) 

Maxxam ID RC1511 

Sample ID RUN 3-BH5-M23/PCB 

Matrix Stack Sampling Train 

Test DescriPtion 

12 3 7 8-TCDF Confirmation (M23) 

IDioxins/Furans in Air (Method 23) 

(PCB Conaeners in Air (1668A) 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

Test Summary 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Instrumentation Batch Extracted Analyzed Analyst 

HRMS/MS 3191218 N/A 2013/04/24 Vica Cioranic 

HRMS/MS 3190066 2013/04/16 2013/04/25 Owen Cosby 

HRMS/MSEC 3182506 2013/04/16 2013/04/24 Cathy Xu 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Instrumentation Batch Extracted Analvzed Analyst 

HRMS/MS 3191218 N/A 2013/04/24 Vica Cioranic 

HRMS/MS 3190066 2013/04/16 2013/04/25 Owen Cosby 

HRMS/MSEC 3182506 2013/04/16 2013/04/24 CathvXu 

Page24 of29 

I 

I 

I 

Ma><xam Analyllcs lnternauonal corporatiOn ota l\llaxxam AnalytiC~~ 6740 C;mpoDBDo Roall, M!$Siisauga, Ontario, L5N as Tel: (905) 817·5700 Tofi·Free: 80()-563·6266 Fax: (905) 817·5777 www.maxxam.oa 
Ma§am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Results relate only to the items tested. 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

GENERAL COMMENTS 

Page25of29 

Ma'xam Analylics International COr!JGration o/a Maxxam Analytlcs 5740 campobello Roaa, MlssiSSa!J;Ia, Ontarlo,L5N 21.8 Tel: (905) 817·5700 Toll-Free: 800.563-6266 fax: (905) 817-5777 www.maxxam.ca 
Maf9am 

QA/QC 

Batch 

Num lnit QC Tvoe 

3182506 cxu Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Method Blank 

Keika Ventures 

Attention: Lorri L White 

Client Project #: Tl1550 

P.O.#: 10244 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Quality Assurance Report 

Maxxam Job Number: GB351227 

Date 

Analyzed 

Parameter ww/mm/dd 

C13-233'44'55'-HeptaCB-(189) 2013/04/24 

C13-233'44'5-HexaCB-(156) 2013/04/24 

C 13-233'44 '5'-HexaCB-( 157) 2013/04/24 

C 13-233'44 '-PentaCB-( 1 05) 2013/04/24 

C 13-23'44'55'-HexaCB-( 167) 2013/04/24 

C 13-2344'5-PentaCB-( 114) 2013/04/24 

C13-23'44'5-PentaCB-(118) 2013/04/24 

C 13-2'344'5-PentaCB-( 123) 2013/04/24 

C13-33'44'55'-HexaCB-(169) 2013/04/24 

C 13-33'44'5-PentaCB-( 126) 2013/04/24 

C13-33'44'-TetraCB-(77) 2013/04/24 

C13-344'5-TetraCB-(81) 2013/04/24 

33'44'-TetraCB-(77) 2013/04/24 

33'44'-TetraCB-(77) 2013/04/24 

344'5-TetraCB-(81) 2013/04/24 

344'5-TetraCB-(81) 2013/04/24 

233'44'-PentaCB-( 1 05) 2013/04/24 

233'44'-PentaCB-(105) 2013/04/24 

2344'5-PentaCB-(114) 2013/04/24 

2344'5-PentaCB-(114) 2013/04/24 

23'44'5-PentaCB-(118) 2013/04/24 

23'44'5-PentaCB-(118) 2013/04/24 

23'44'5'-PentaCB-(123) 2013/04/24 

23'44'5'-PentaCB-(123) 2013/04/24 

33'44'5-PentaCB-(126) 2013/04/24 

33'44'5-PentaCB-(126) 2013/04/24 

HexaCB-( 156)+( 157) 2013/04/24 

HexaCB-( 156)+( 157) 2013/04/24 

23'44'55'-HexaCB-(167) 2013/04/24 

23'44'55'-HexaCB-(167) 2013/04/24 

33'44'55'-HexaCB-(169) 2013/04/24 

33'44'55'-HexaCB-(169) 2013/04/24 

233'44'55'-HeptaCB-( 189) 2013/04124 

233'44'55'-HeptaCB-( 189) 2013/04/24 

C13-233'44'55'-HeptaCB-( 189) 2013/04124 

C13-233'44'5-HexaCB-(156) 2013/04124 

C13-233'44'5'-HexaCB-(157) 2013/04/24 

C13-233'44'-PentaCB-( 1 05) 2013/04/24 

C13-23'44'55'-HexaCB-( 167) 2013/04/24 

C13-2344'5-PentaCB-( 114) 2013/04/24 

C13-23'44'5-PentaCB-(118) 2013/04/24 

C13-2'344'5-PentaCB-( 123) 2013/04/24 

C13-33'44'55'-HexaCB-( 169) 2013/04/24 

C13-33'44'5-PentaCB-(126) 2013/04/24 

C13-33'44'-TetraCB-(77) 2013/04/24 

C13-344'5-TetraCB-(81) 2013/04/24 

33'44'-TetraCB-(77) 2013/04/24 

344'5-TetraCB-(81) 2013/04/24 

233'44'-PentaCB-(1 05) 2013/04/24 

2344'5-PentaCB-(114) 2013/04/24 

23'44'5-PentaCB-(118) 2013/04/24 

23'44'5'-PentaCB-(123) 2013/04/24 

33'44'5-PentaCB-( 126) 2013/04/24 

HexaCB-( 156)+( 157) 2013/04/24 

23'44'55'-HexaCB-(167) 2013/04/24 

Page 26 of29 

Value %Recoverv 

98 

108 

108 

111 

107 

108 

108 

107 

104 

120 

112 

107 

98 

0 

99 

0 

99 

1.0 

96 

1.0 

98 

3.0 

99 

1.0 

93 

4.2 

100 

1.0 

100 

0 

102 

0 

93 

2.1 

102 

115 

115 

115 

111 

115 

113 

113 

106 

123 

116 

113 

<0.037, EDL=0.037 

<0.037, EDL=0.037 

<0.030, EDL=0.030 

<0.028, EDL=0.028 

<0.030, EDL=0.030 

<0.031, EDL=0.031 

<0.029, EDL=0.029 

<0.036, EDL=0.036 

<0.039, EDL=0.039 

Units QC Limits 

% 20-150 

% 20-150 

% 20-150 

% 20- 150 

% 20- 150 

% 20- 150 

% 20- 150 

% 20- 150 

% 20- 150 

% 20-150 

% 20-150 

% 20-150 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% 20 

% N/A 

% N/A 

% 20-150 

% 20- 150 

% 20- 150 

% 20- 150 

% 20- 150 

% 20- 150 

% 20- 150 

% 20-150 

% 20-150 

% 20-150 

% 20- 150 

% 20-150 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

Maxxam Analytics lrnernatlonal Corporation o/a Maxxam AnalyticS 6740 campobePo Road, Mlsslssauga, Ontario, L5N 21..8 Tel: (905) 817-5700 Toll-Free: SOQ-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma-§am 

QAIQC 

Batch 

Num lnit QC Tvoe 

3182506 cxu Method Blank 

3190066 OBC Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Method Blank 

Keika Ventures 

Attention: Lorri L White 

Client Project #: Tl1550 

P.O.#: 10244 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Quality Assurance Report (Continued) 

Maxxam Job Number: GB351227 

Date 

Analyzed 

Parameter vvvv/mm/dd 

33'44'55'-HexaCB-(169) 2013/04/24 

233'44'55'-HeptaCB-( 189) 2013/04/24 

C13-1234678 HeptaCDD 2013/04/25 

C13-1234678 HeptaCDF 2013/04/25 

C13-123678 HexaCDD 2013/04/25 

C13-123678 HexaCDF 2013/04/25 

C13-12378 PentaCDD 2013/04/25 

C13-12378 PentaCDF 2013/04/25 

C13-123789 HexaCDF 2013/04/25 

C13-2378 TetraCDD 2013/04/25 

C13-2378 TetraCDF 2013/04/25 

C13-0ctachlorodibenzo-p-Dioxin 2013/04/25 

2,3,7,8-Tetra COD 2013/04/25 

2,3,7,8-Tetra COD 2013/04/25 

1 ,2,3, 7 ,8-Penta COD 2013/04/25 

1 ,2,3,7,8-Penta COD 2013/04/25 

1,2,3,4,7,8-Hexa COD 2013/04/25 

1 ,2,3,4, 7 ,8-Hexa COD 2013/04/25 

1 ,2,3,6,7,8-Hexa COD 2013/04/25 

1 ,2,3,6,7,8-Hexa COD 2013/04/25 

1,2,3, 7 ,8,9-Hexa COD 2013/04/25 

1 ,2,3, 7 ,8,9-Hexa COD 2013/04/25 

1 ,2,3,4,6, 7 ,8-Hepta COD 2013/04/25 

1,2,3,4,6,7,8-Hepta COD 2013/04/25 

1,2,3,4,6,7,8,9-0cta CDD 2013/04/25 

1,2,3,4,6,7,8,9-0cta COD 2013/04/25 

2,3,7,8-Tetra CDF 2013/04/25 

2,3,7,8-Tetra CDF 2013/04/25 

1,2,3, 7 ,8-Penta CDF 2013/04/25 

1,2,3,7,8-Penta CDF 2013/04/25 

2,3,4,7,8-Penta CDF 2013/04/25 

2,3,4,7,8-Penta CDF 2013/04/25 

1,2,3,4,7,8-Hexa CDF 2013/04/25 

1 ,2,3,4,7,8-Hexa CDF 2013/04/25 

1,2,3,6,7,8-Hexa CDF 2013/04/25 

1 ,2,3,6,7,8-Hexa CDF 2013/04/25 

2,3,4,6,7,8-Hexa CDF 2013/04/25 

2,3,4,6,7,8-Hexa CDF 2013/04/25 

1,2,3,7,8,9-Hexa CDF 2013104/25 

1,2,3,7,8,9-Hexa CDF 2013/04/25 

1 ,2,3,4,6, 7 ,8-Hepta CDF 2013104/25 

1 ,2,3,4,6, 7 ,8-Hepta CDF 2013104/25 

1 ,2,3,4, 7 ,8,9-Hepta CDF 2013104/25 

1 ,2,3,4, 7 ,8,9-Hepta CDF 2013/04/25 

1 ,2,3,4,6, 7 ,8,9-0cta CDF 2013/04/25 

1 ,2,3,4,6, 7 ,8,9-0cta CDF 2013/04/25 

C13-1234678 HeptaCDD 2013/04/25 

C13-1234678 HeptaCDF 2013/04/25 

C13-123678 HexaCDD 2013/04/25 

C13-123678 HexaCDF 2013/04/25 

C13-12378 PentaCDD 2013/04/25 

C13-12378 PentaCDF 2013/04/25 

C13-123789 HexaCDF 2013/04/25 

C13-2378 TetraCDD 2013/04/25 

C13-2378 TetraCDF 2013/04/25 

Page 27 of29 

Value %Recoverv 

<0.040, EDL=0.040 

<0.014, EDL=0.014 

115 

115 

77 

70 

70 

68 

73 

41 

57 

100 

113 

NC 

118 

NC 

98 

NC 

109 

NC 

131 

NC 

98 

NC 

95 

NC 

99 

NC 

104 

NC 

114 

NC 

103 

NC 

115 

NC 

122 

NC 

127 

NC 

90 

NC 

87 

NC 

99 

NC 

119 

114 

72 

71 

67 

69 

75 

45 

66 

Units QC Limits 

ng 

ng 

% 25- 130 

% 25- 130 

% 40- 130 

% 40- 130 

% 40- 130 

% 40-130 

% 40-130 

% 40- 130 

% 40-130 

% 25- 130 

% 80-140 

% 20 

% 80- 140 

% 20 

% 80- 140 

% 20 

% 80- 140 

% 20 

% 80- 140 

% 20 

% 80- 140 

% 20 

% 80-140 

% 20 

% 80-140 

% 20 

% 80-140 

% 20 

% 80- 140 

% 20 

% 80-140 

% 20 

% 80-140 

% 20 

% 80- 140 

% 20 

% 80-140 

% 20 

% 80-140 

% 20 

% 80-140 

% 20 

% 80- 140 

% 20 

% 25- 130 

% 25- 130 

% 40- 130 

% 40- 130 

% 40-130 

% 40- 130 

% 40- 130 

% 40- 130 

% 40- 130 

Maxxam Analyucs Jrnernational COrporation ala Maxxam Anal}'lics 6740 campobello Roaa, MISslssauga, Ontario, L5N 21..8 Tel: (905) 817-5700 Toll-Free: aoo-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
rv1a(52am 

QNQC 

Batch 

Num lnit QC Type 

3190066 OBC Method Blank 

3191218 VCI Method Blank 

Keika Ventures 

Attention: Lorri L White 

Client Project#: Tl1550 

P.O.#: 10244 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Quality Assurance Report (Continued) 

Maxxam Job Number: GB351227 

Date 

Analyzed 

Parameter yyyy/mm/dd 

C 13-0ctachlorodibenzo-p-Dioxin 2013/04/25 

2,3,7,8-Tetra COD 2013/04/25 

1,2,3,7,8-Penta COD 2013/04/25 

1 ,2,3,4, 7 ,8-Hexa COD 2013/04/25 

1 ,2,3,6, 7 ,8-Hexa COD 2013/04/25 

1 ,2,3,7,8,9-Hexa COD 2013/04/25 

1 ,2,3,4,6, 7 ,8-Hepta COD 2013/04/25 

1 ,2,3,4,6, 7 ,8,9-0cta COD 2013/04/25 

Total Tetra COD 2013/04/25 

Total Penta COD 2013/04/25 

Total Hexa COD 2013/04/25 

Total Hepta COD 2013/04/25 

2,3,7,8-Tetra CDF 2013/04/25 

1 ,2,3, 7 ,8-Penta CDF 2013/04/25 

2,3,4,7,8-Penta CDF 2013/04/25 

1 ,2,3,4,7,8-Hexa CDF 2013/04/25 

1 ,2,3,6,7,8-Hexa CDF 2013/04/25 

2,3,4,6,7,8-Hexa CDF 2013/04/25 

1 ,2,3, 7 ,8,9-Hexa CDF 2013/04/25 

1 ,2,3,4,6, 7 ,8-Hepta CDF 2013/04/25 

1 ,2,3,4,7,8,9-Hepta CDF 2013/04/25 

1 ,2,3,4,6, 7 ,8,9-0cta CDF 2013/04/25 

Total Tetra CDF 2013/04/25 

Total Penta CDF 2013/04/25 

Total Hexa CDF 2013/04/25 

Total Hepta CDF 2013/04/25 

Confirmation C13-2378 TetraCDF 2013/04/24 

Confirmation 2 3 7 8-Tetra CDF 2013/04/24 

Value %Recoverv 

119 

<6.7, EDL=6.7 

<7.4, EDL=7.4 

<6.5, EDL=6.5 

<6.3, EDL=6.3 

<6.4, EDL=6.4 

<7.4, EDL=7.4 

<6.4, EDL=6.4 

<6.7, EDL=6.7 

<7.4, EDL=7.4 

<6.4, EDL=6.4 

<7.4, EDL=7.4 

<2.9, EDL=2.9 

<7.0, EDL=7.0 

<6.6, EDL=6.6 

<3.0, EDL=3.0 

<2.9, EDL=2.9 

<3.6, EDL=3.6 

<4.0, EDL=4.0 

<3.6, EDL=3.6 

<4.9. EDL=4.9 

<7.1, EDL=7.1 

<2.9, EDL=2.9 

<6.8, EDL=6.8 

<3.3, EDL=3.3 

<4.1, EDL=4.1 

61 

<3.2 EDL=3.2 

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

Units QC Limits 

% 25- 130 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

pg 

% 40- 135 

pq 

Spiked Blank: A blank matrix sample to which a known amount of the analyte, usually from a second source, has been added. Used to evaluate method 

accuracy. 

Method Blank: A blank matrix containing all reagents used in the analytical procedure. Used to identify laboratory contamination. 

Surrogate: A pure or isotopically labeled compound whose behavior mirrors the analytes of interest. Used to evaluate extraction efficiency. 

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 28 of29 

!Vlaxxam Ana!ylics lrrternalional COrporation o!a Maxxam Analytics 6740 Canpobello Road, MlSsissauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: {905) 817-5777 wwvv.maxxam.ca 
Validation Signature Page 

Maxxam Job #: 8351227 

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

Branko Vrzic, A.SC.T., Senior Analyst, HRMS Services 

/(u .)lhLUU 

Kay sr::& C. Chern, Scientific Specialist, HRMS Sen<lc.,; 

Maxxam has procedures in place to guard against improper use of the electronic signature and have the required "signatories", as per section 5.1 0.2 of 

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

Page29 of29 

1\ilaxxam Analylics International COrporation o/a Maxxam Analytlcs 6740 C;mpot>ello Road, MISSiSsauga, On!arlo, L5N 2L8 Tel: (905) 817-5700 Toll-Free: 80Q-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Your P.O.#: 10244 

Your Project#: Tl1550 

Attention: Lorri L White 

Keika Ventures 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

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

Chapel Hill 

101 Strangford Lane 

Durham, NC 

USA 27713 

Report Date: 2013/05/02 

CERTIFICATE OF ANALYSIS 

MAXXAM JOB#: 8351259 

Received: 2013/04/06, 13:00 

Sample Matrix: Stack Sampling Train 

#Samples Received: 7 

Analyses 

PAH's in Air (CARB429) 

Date Date 

Quantity Extracted Analyzed Laboratory Method 

7 2013/04/16 2013/05/01 BRL SOP-00418 

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

Encryption Key~ 1 Ancy Sebastian 

L$_,l;Pdw- 02 May 2013 16:52:06 -04:00 

Please direct all qut:::suv11::s '"'tl"''u'"tl '"'"Certificate of Analysis to your Project Manager. 

Ancy Sebastian, C. Tech., Senior Project Manager, Air Taxies 

Email: ASebastian@maxxam.ca 

Phone# (905) 817-5831 

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

Method 

Reference 

GARB 429mod(CARB429) 

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

5.1 0.2 of ISO/IEC 17025:2005(E), signing the reports. For Service Group specific validation please refer to the Validation Signature Page. 

Maxxam Analytics Inc. is a NELAC accredited laboratory. Certificate # CANA001. Use of the NELAC logo however does not insure that 

Maxxam is accredited for all of the methods indicated. This certificate shall not be reproduced except in full, without the written approval of 

Maxxam Analytics Inc. Maxxam has procedures in place to guard against improper use of the electronic signature and have the required 

"signatories", as per section. 

Total cover pages: 1 

Page 1 of 12 

Ma-.::xarn 1\na!ytlcs lmernational Corporation o/a Maxxam Analy"tics 67<10 Campobello Road, Mlssissauga, ontario, L5N 2L8 Tel: (905i 817-5700 Toll-Free: 800-563-6266 Fax: (905,) 817-5777\,.VWW.m~xanu.:a 
Maxxam Job #: 8351259 

Report Date: 2013/05/02 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1605 RC1606 RC1607 

Sampling Date 2013/03/14 2013/03/18 2013/03/18 

00:01 00:01 00:01 

COC Number N/A N/A N/A 

Units TRAIN FDL RDL RUN 1-BH2-PAH EDL RDL RUN 2-BH2·PAH 

BLANK-PAH 

Naphthalene ng 761 24 10 27400 (1) 1400 500 48800 (1) 

2-Methylnaphthalene ng 329 18 10 21700 490 500 42900 (1) 

2-Chloronaphthalene ng <1.8 1.8 10 46.6 1.2 10 94.2 

Acenaphthylene ng <35 35 10 2600 140 500 3060 

Acenaphthene ng <62 62 10 1730 940 500 2230 

Fluorene ng 166 20 10 2230 300 500 3290 

Phenanthrene ng 435 23 10 13400 480 500 25100 (1) 

Anthracene ng <27 27 10 1040 570 500 1180 

Fluoranthene ng 19.6 6.8 10 11100 590 500 73500 (1) 

Pyrene ng 10.9 6.3 10 5200 550 500 42700 (1) 

Benzo(a)anthracene ng <5.9 5.9 10 618 150 500 3260 

Chrysene ng <6.1 6.1 10 3660 140 500 29000 (1) 

Benzo(b )fluoranthene ng <2.0 2.0 10 503 60 500 3320 

Benzo(k)fluoranthene ng <3.3 3.3 10 172 35 10 1310 

Benzo( e )pyrene ng <4.8 4.8 10 364 30 10 1950 

Benzo(a)pyrene ng <6.1 6.1 10 <37 37 10 <60 

Perylene ng <3.5 3.5 10 <33 33 10 <55 

lndeno(1 ,2,3-cd)pyrene ng <5.2 5.2 10 27.7 6.8 10 71.3 

Dibenz(a,h )anthracene ng <3.9 3.9 10 <4.7 4.7 10 9.6 

Benzo(g,h,i)perylene ng <4.7 4.7 10 36.4 6.7 10 81.5 

Coronene ng <10 10 10 12.6 2.9 10 23.6 

Surrogate Recovery (%) 

2-Methylnaphthalene-2H 1 0 % 66 NtA N/A 55 N/A N/A 43 (2) 

Acenaphthylene-2H8 % 64 NtA N/A 78 N/A N/A 67 

Anthracene-2H1 0 % 42 (2) NtA N/A 95 N/A N/A 72 

Benz(a)anthracene-2H12 % 98 NtA N/A 74 N/A N/A 142 

Benzo(a)pyrene-2H12 % 48 (2) NtA N/A 93 N/A N/A 90 

Benzo(b )fluoranthene-2H 12 % 76 NtA N/A 109 N/A N/A 91 

Benzo(g,h,i)perylene-2H12 % 54 NtA N/A 97 N/A N/A 96 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch= Quality Control Batch 

( 1 ) EMCL - PAH analysis - Exceeds Maximum Calibration Limit 

EDL RDL QC Batch 

700 500 3182508 

300 500 3182508 

1.2 10 3182508 

66 500 3182508 

550 500 3182508 

190 500 3182508 

390 500 3182508 

450 500 3182508 

550 500 3182508 

510 500 3182508 

130 500 3182508 

180 500 3182508 

45 500 3182508 

87 500 3182508 

58 500 3182508 

60 10 3182508 

55 10 3182508 

9.0 10 3182508 

4.5 10 3182508 

9.5 10 3182508 

4.3 10 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

( 2) Recovery or RPD for this parameter is outside control limits. The overall quality control for this analysis meets acceptability criteria. 

Page 2 of 12 

Maxxam Analyucs lrnernational COrporation ola Maxxam Analytics 6740 CampobeHo Road, MlssiSsauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: SOQ-563-6266 Fax: (905) 817·5777 www.maxxam.ca 
Maxxam Job #: 8351259 

Report Date: 2013/05/02 

Keika Ventures 

Client Project #: Tl1550 

Site location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1605 RC1606 RC1607 

!Sampling Date 2013/03/14 2013/03/18 2013/03/18 

00:01 00:01 00:01 

COG Number N/A N/A N/A 

Units TRAIN DL RDL RUN 1-BH2-PAH EDL RDL RUN 2-BH2-PAH 

BLANK-PAH 

Benzo(k}fluoranthene-2H12 % 75 N/A N/A 98 N/A N/A 65 

Chrysene-2H 12 % 80 N/A N/A 59 N/A N/A 91 

Dibenzo( a,h )anthracene-2H 14 % 53 N/A N/A 115 N/A N/A 120 

Fluoranthene-2H1 0 % 79 N/A N/A 88 N/A N/A 88 

Fluorene-2H 1 0 % 123 N/A N/A 70 N/A N/A 68 

lndeno(1,2,3-c,d}pyrene-2H12 % 51 N/A N/A 98 N/A N/A 103 

Naphthalene-2H8 % 71 N/A N/A 46 (1} N/A N/A 35 (1} 

Perylene-2H12 % 54 N/A N/A 83 N/A N/A 75 

Phenanthrene-2H 1 0 % 44 (1} N/A N/A 110 N/A N/A 105 

Terphenyi-2H14 % 108 N/A N/A 137 N/A N/A 153 (1} 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

EDL RDL pc Batch 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

( 1 ) Recovery or RPD for this parameter is outside control limits. The overall quality control for this analysis meets acceptability criteria. 

Page 3 of 12 

Maxxam Analytics lmernational COrporation o!a Max.xam Analytlcs 6740 Campobello Road, Mtsslssauga, On!arlo, L5N 21..8 Tel: (905) 817·5700 TOll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Maxxam Job #: 8351259 

Report Date: 2013/05/02 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1608 RC1609 RC1610 

Sampling Date 2013/03/18 2013/03/14 2013/03/14 

00:01 00:01 00:01 

OC Number N/A N/A N/A 

Units RUN 3-BH2-PAH EDL RUN 1-BH5-PAH EDL RDL RUN 2-BH5-PAH 

Naphthalene ng 43800 (1) 480 45100 (1) 330 500 28600 (1) 

2-Methylnaphthalene ng 29700 (1) 310 19200 120 500 15900 

2-Chloronaphthalene ng 92.6 0.84 81.0 0.40 10 72.8 

Acenaphthylene ng 4570 67 9040 89 500 4780 

Acenaphthene ng 2520 490 4030 330 500 2680 

Fluorene ng 3480 170 5080 220 500 2950 

Phenanthrene ng 22400 230 67100 (1) 430 500 53400 (1) 

Anthracene ng 1630 270 2170 500 500 2650 

Fluoranthene ng 15100 440 45700 (1) 310 500 43000 (1) 

Pyrene ng 7790 410 23000 290 500 26600 

Benzo(a )anthracene ng 672 69 1210 110 500 1300 

Chrysene ng 3830 80 6850 120 500 4500 

Benzo(b )fluoranthene ng 902 30 956 120 500 466 

Benzo(k)fluoranthene ng 246 15 344 16 10 135 

Benzo( e )pyrene ng 519 33 1150 230 500 477 

Benzo(a)pyrene ng 21 16 <27 27 10 <16 

Perylene ng <15 15 <18 18 10 <11 

lndeno(1 ,2,3-cd)pyrene ng 52.4 7.0 50.6 6.6 10 16.6 

Dibenz( a,h )anthracene ng 9.6 3.5 8.5 3.8 10 <2.8 

Benzo(g,h,i)perylene ng 64.5 7.0 58.9 6.9 10 25.2 

Coronene ng 44.7 4.3 32.2 4.2 10 12.8 

Surrogate Recovery(%) 

2-Methylnaphthalene-2H 1 0 % 47 (2) N/A 47 (2) N/A N/A 49 (2) 

Acenaphthylene-2H8 % 62 N/A 52 N/A N/A 57 

Anthracene-2H1 0 % 69 N/A 55 N/A N/A 53 

Benz(a)anthracene-2H12 % 127 N/A 95 N/A N/A 107 

Benzo(a)pyrene-2H12 % 107 N/A 65 N/A N/A 54 

Benzo(b )fluoranthene-2H12 % 111 N/A 111 N/A N/A 115 

Benzo(g,h,i)perylene-2H12 % 103 N/A 98 N/A N/A 92 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

( 1 ) EMCL - PAH analysis - Exceeds Maximum Calibration Limit 

EDL RDL QC Batch 

320 500 3182508 

130 500 3182508 

1.2 10 3182508 

49 500 3182508 

320 500 3182508 

150 500 3182508 

330 500 3182508 

390 500 3182508 

320 500 3182508 

300 500 3182508 

72 500 3182508 

94 500 3182508 

5.4 10 3182508 

9.1 10 3182508 

13 10 3182508 

16 10 3182508 

11 10 3182508 

3.6 10 3182508 

2.8 10 3182508 

3.7 10 3182508 

2.6 10 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

( 2) Recovery or RPD for this parameter is outside control limits. The overall quality control for this analysis meets acceptability criteria. 

Page 4 of 12 

lllla•xam Analylics lrrternalional COrporation o:a Maxxam Analylics 6740 C<mpobello Road, Mfsslssauga, Ontario, L5N 21..8 Tel: (905) 817-5700 Toll-Free: SOQ-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Maxxam Job #: 8351259 

Report Date: 2013/05/02 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1608 RC1609 RC1610 

Sampling Date 2013/03/18 2013/03/14 2013/03/14 

00:01 00:01 00:01 

COC Number N/A N/A N/A 

Units RUN 3-BH2-PAH EDL RUN 1-BH5-PAH EDL RDL RUN 2-BH5-PAH 

Benzo(k)fluoranthene-2H 12 % 101 N/A 86 N/A N/A 88 

Chrysene-2H 12 % 85 N/A 70 N/A N/A 87 

Dibenzo( a,h )anthracene-2H 14 % 137 N/A 130 N/A N/A 126 

Fluoranthene-2H 1 0 % 88 N/A 99 N/A N/A 99 

Fluorene-2H 1 0 % 66 N/A 70 N/A N/A 72 

lndeno( 1,2,3-c,d)pyrene-2H 12 % 114 N/A 110 N/A N/A 105 

Naphthalene-2H8 % 34 (1) N/A 33 (1) N/A N/A 42 (1) 

Perylene-2H 12 % 80 N/A 61 N/A N/A 57 

Phenanthrene-2H 1 0 % 92 N/A 97 N/A N/A 112 

Terphenyi-2H14 % 151 (1) N/A 159 (1) N/A N/A 168 (1) 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

I=DL RDL QC Batch 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

N/A N/A 3182508 

( 1 ) Recovery or RPD for this parameter is outside control limits. The overall quality control for this analysis meets acceptability criteria. 

Page 5 of 12 

l\iianam Analytics lrnernational Corporation o/a Ma""am Analy!lcs 6740 Campobello ROO!I, Mlsslssauga, Ontario, L5N 2L8 Tel: (905) 817·5700 Toll-Free: SOD-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Maxxam Job #: 8351259 

Report Date: 2013/05/02 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1611 

Sampling Date 2013/03/14 

00:01 

COC Number N/A 

Units RUN 3-BH5·PAH EDL RDL CJC Batch 

Naphthalene ng 31100 (1) 330 500 3182508 

2-Methylnaphthalene ng 19100 130 500 3182508 

2-Chloronaphthalene ng 52.5 0.27 10 3182508 

Acenaphthylene ng 3760 51 500 3182508 

Acenaphthene ng 2370 270 500 3182508 

Fluorene ng 2280 200 500 3182508 

Phenanthrene ng 36900 (1) 120 500 3182508 

Anthracene ng 1360 140 500 3182508 

Fluoranthene ng 18200 130 500 3182508 

Pyrene ng 9510 120 500 3182508 

Benzo(a)anthracene ng 494 5.6 10 3182508 

Chrysene ng 1620 68 500 3182508 

Benzo(b )fluoranthene ng 266 3.0 10 3182508 

Benzo(k)fluoranthene ng 92.7 5.4 10 3182508 

Benzo(e)pyrene ng 273 8.1 10 3182508 

Benzo(a)pyrene ng <10 10 10 3182508 

Perylene ng <7.2 7.2 10 3182508 

lndeno(1 ,2,3-cd)pyrene ng 8.0 2.4 10 3182508 

Dibenz(a,h )anthracene ng <2.0 2.0 10 3182508 

Benzo(g,h,i)perylene ng 10.9 2.5 10 3182508 

Coronene ng 6.1 2.2 10 3182508 

Surrogate Recovery (%) 

2-Methylnaphthalene-2H10 % 42 (2) N/A N/A 3182508 

Acenaphthylene-2H8 % 61 N/A N/A 3182508 

Anthracene-2H1 0 % 51 N/A N/A 3182508 

Benz(a)anthracene-2H 12 % 174 (2) N/A N/A 3182508 

Benzo(a)pyrene-2H12 % 54 N/A N/A 3182508 

Benzo(b )fluoranthene-2H 12 % 128 N/A N/A 3182508 

Benzo(g,h,i)perylene-2H 12 % 100 N/A N/A 3182508 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

( 1 ) EMCL - PAH analysis - Exceeds Maximum Calibration Limit 

( 2) Recovery or RPD for this parameter is outside control limits. The overall 

quality control for this analysis meets acceptability criteria. 

Page 6 of 12 

:Vlauam Analylics lrnemational COrporation ola Maxxam Analytics 6740 Campobello Road. Mlsslssauga. Ontario. L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Maxxam Job #: 8351259 

Report Date: 2013/05/02 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. -FELMAN PRODUCTIONS 

Your P.O.#: 10244 

RESULTS OF ANALYSES OF STACK SAMPLING TRAIN 

Maxxam ID RC1611 

~ampling Date 2013/03/14 

00:01 

COC Number N/A 

Units RUN 3-BH5-PAH EDL RDL DC Batch 

Benzo(k)fluoranthene-2H12 % 94 N/A N/A 3182508 

Chrysene-2H 12 % 112 N/A N/A 3182508 

Dibenzo(a,h )anthracene-2H 14 % 132 N/A N/A 3182508 

Fluoranthene-2H1 0 % 88 N/A N/A 3182508 

Fluorene-2H 1 0 % 79 N/A N/A 3182508 

lndeno(1,2,3-c,d)pyrene-2H 12 % 112 N/A N/A 3182508 

Naphthalene-2H8 % 35 (1) N/A N/A 3182508 

Perylene-2H12 % 56 N/A N/A 3182508 

Phenanthrene-2H 1 0 % 104 N/A N/A 3182508 

Terphenyi-2H14 % 153 (1) N/A N/A 3182508 

N/A =Not Applicable 

RDL = Reportable Detection Limit 

EDL = Estimated Detection Limit 

QC Batch = Quality Control Batch 

( 1 ) Recovery or RPD for this parameter is outside control limits. The overall 

quality control for this analysis meets acceptability criteria. 

Page 7 of 12 

l';laxxam Analylics lmernalional COrporation o/a Maxxam Anal~>tics 6740 GampobeHo Roao, Mlsslssauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: BOQ-563-6266 Fa>:: (905) 811-5777 www.mro:xam.ca 
f\/1 e:~ ~a rn 

Keika Ventures 

Maxxam Job #: 8351259 Client Project #: Tl1550 

Report Date: 2013/05/02 Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

Test Summary 

Maxxam ID RC1605 Collected 2013/03/14 

Sample ID TRAIN BLANK-PAH Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

HRMS/MS 3182508 2013/04/16 2013/05/01 Edmond Mcneil 

Maxxam ID RC1606 Collected 2013/03/18 

Sample ID RUN 1-BH2-PAH Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

HRMS/MS 3182508 2013/04/16 2013/05/01 Edmond Mcneil 

Maxxam ID RC1607 Collected 2013/03/18 

Sample ID RUN 2-BH2-PAH Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

HRMS/MS 3182508 2013/04/16 2013/05/01 Edmond Mcneil 

Maxxam ID RC1608 Collected 2013/03/18 

Sample ID RUN 3-BH2-PAH Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

HRMS/MS 3182508 2013/04/16 2013/05/01 Edmond Mcneil 

Maxxam ID RC1609 Collected 2013/03/14 

Sample ID RUN 1-BH5-PAH Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

HRMS/MS 3182508 2013/04/16 2013/05/01 Edmond Mcneil 

Maxxam ID RC1610 Collected 2013/03/14 

Sample ID RUN 2-BH5-PAH Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted Anal zed Anal st 

HRMS/MS 3182508 2013/04/16 2013/05/01 Edmond Mcneil 

Maxxam ID RC1611 Collected 2013/03/14 

Sample ID RUN 3-BH5-PAH Shipped 

Matrix Stack Sampling Train Received 2013/04/06 

Instrumentation Batch Extracted 

HRMS/MS 3182508 2013/04/16 

Page 8 of 12 

Maxxam Analyties !rnernational COrporatiOn o/a Maxxam Analytlcs 6740 CampobeHo Road, Mlsslssauga, OntariO, L5N 2L8 Tel: (905) 817-5700 Toll-Free: SOQ-563-6266 Fax: (905) 817-5777 www.maxxam.<"' 
Ma§am 

Maxxam Job #: 8351259 

Report Date: 2013/05/02 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

GENERAL COMMENTS 

PAH Analysis: Some of the recoveries are outside of standard limits 50% -150-% due to matrix suppression. 

Results relate onlv to the items tested. 

Page 9 of 12 

Maxxam Ana!y!ics International Corporation o!a Maxxam Analy!ics 6740 carnpobeno Road, Mlsslssauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-free: 800.563-6266 Fax: (905) 817-5777 www.maxxam.ca 
QA/QC 

Batch 

Num lnit QCTvoe 

3182508 EM Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

RPD 

Spiked Blank 

Keika Ventures 

Attention: Lorri L White 

Client Project#: Tl1550 

P.O.#: 10244 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Quality Assurance Report 

Maxxam Job Number: GB351259 

Date 

Analyzed 

Parameter ww/mm/dd 

2-Methylnaphthalene-2H1 0 2013/04/30 

Acenaphthylene-2H8 2013/04/30 

Benz(a)anthracene-2H 12 2013/04/30 

Benzo(a)pyrene-2H12 2013/04/30 

Benzo(b )fluoranthene-2H 12 2013/04/30 

Benzo(g,h,i)perylene-2H12 2013/04/30 

Benzo(k)fluoranthene-2H12 2013/04/30 

Chrysene-2H12 2013/04/30 

Dibenzo(a,h)anthracene-2H 14 2013/04/30 

Fluoranthene-2H1 0 2013/04/30 

lndeno(1 ,2,3-c,d)pyrene-2H12 2013/04/30 

Naphthalene-2H8 2013/04/30 

Perylene-2H12 2013/04/30 

Phenanthrene-2H 10 2013/04/30 

Naphthalene 2013/04/30 

Naphthalene 2013/04/30 

2-Methylnaphthalene 2013/04/30 

2-Methylnaphthalene 2013/04/30 

2-Chloronaphthalene 2013/04/30 

2-Chloronaphthalene 2013/04/30 

Acenaphthylene 2013/04/30 

Acenaphthylene 2013/04/30 

Acenaphthene 2013/04/30 

Acenaphthene 2013/04/30 

Fluorene 2013/04/30 

Fluorene 2013/04/30 

Phenanthrene 2013/04/30 

Phenanthrene 2013/04/30 

Anthracene 2013/04/30 

Anthracene 2013/04/30 

Fluoranthene 2013/04/30 

Fluoranthene 2013/04/30 

Pyrene 2013/04/30 

Pyrene 2013/04/30 

Benzo(a)anthracene 2013/04/30 

Benzo(a)anthracene 2013/04/30 

Chrysene 2013/04/30 

Chrysene 2013/04/30 

Benzo(b )fluoranthene 2013/04/30 

Benzo(b )fluoranthene 2013/04/30 

Benzo(k)fluoranthene 2013/04/30 

Benzo(k)fluoranthene 2013/04/30 

Benzo( e )pyrene 2013/04/30 

Benzo( e )pyrene 2013/04/30 

Benzo(a)pyrene 2013/04/30 

Benzo(a)pyrene 2013/04/30 

Perylene 2013/04/30 

Perylene 2013/04/30 

lndeno(1 ,2,3-cd)pyrene 2013/04/30 

lndeno(1 ,2,3-cd)pyrene 2013/04/30 

Dibenz(a,h)anthracene 2013/04/30 

Dibenz(a,h )anthracene 2013/04/30 

Benzo(g,h,i)perylene 2013/04/30 

Benzo(g,h,i)perylene 2013/04/30 

Coronene 2013/04/30 

Page 10 of 12 

Value %Recoverv 

84 

73 

91 

81 

86 

64 

93 

77 

64 

86 

67 

99 

77 

53 

283 (1) 

7.3 (1) 

111 

0.9 

85 

4.8 

110 

2.7 

110 

1.8 

169 (1) 

17.4 (1) 

111 

1.8 

98 

11.5 

109 

10.6 

103 

5.0 

106 

0 

132 

5.2 

107 

1.9 

98 

16.6 

115 

5.4 

79 

3.7 

110 

1.8 

131 

12.1 

124 

2.4 

134 

0.7 

126 

Units QC Limits 

% 50- 150; 

% 50 -150; 

% 50-150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50-150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50- 150 

% 60-140 

% 50 

% 60- 140 

% 50 

% N/A 

% 50 

% 60- 140 

% 50 

% 60- 140 

% 50 

% 60-140 

% 50 

% 60- 140 

% 50 

% 60-140 

% 50 

% 60- 140 

% 50 

% 60-140 

% 50 

% 60-140 

% 50 

% 60-140 

% 50 

% 60-140 

% 50 

% 60-140 

% 50 

% 60-140 

% 50 

% 60- 140 

% 50 

% 60-140 

% 50 

% 60- 140 

% 50 

% 60- 140 

% 50 

% 60- 140 

% 50 

% N/A 

Ma'xam ''nalylics lmernati<mal corporation ala Maxxam Anal~'lics 6740 campobello Road, MlssiSsauga, Ontario, L5N 2LB Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
lV1a§am 

QNQC 

Batch 

Num lnit QC Tvoe 

3182508 EM RPD 

Method Blank 

Keika Ventures 

Attention: Lorri L White 

Client Project #: Tl1550 

P.O.#: 10244 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Quality Assurance Report (Continued) 

Maxxam Job Number: GB351259 

Date 

Analyzed 

Parameter vvvv/mm/dd 

Coronene 2013/04/30 

2-Methylnaphthalene-2H1 0 2013/04/30 

Acenaphthylene-2H8 2013/04/30 

Benz(a)anthracene-2H 12 2013/04/30 

Benzo(a)pyrene-2H12 2013/04/30 

Benzo(b )fluoranthene-2H 12 2013/04/30 

Benzo(g,h,i)perylene-2H12 2013/04/30 

Benzo(k)fluoranthene-2H12 2013/04/30 

Chrysene-2H12 2013/04/30 

Dibenzo(a,h )anthracene-2H 14 2013/04/30 

Fluoranthene-2H 1 0 2013/04/30 

lndeno( 1 ,2,3-c,d)pyrene-2H12 2013/04/30 

Naphthalene-2H8 2013/04/30 

Perylene-2H 12 2013/04/30 

Phenanthrene-2H 10 2013/04/30 

Naphthalene 2013/04/30 

2-Methylnaphthalene 2013/04/30 

2-Chloronaphthalene 2013/04/30 

Acenaphthylene 2013/04/30 

Acenaphthene 2013/04/30 

Fluorene 2013/04/30 

Phenanthrene 2013/04/30 

Anthracene 2013/04/30 

Fluoranthene 2013/04/30 

Pyrene 2013/04/30 

Benzo(a)anthracene 2013/04/30 

Chrysene 2013/04/30 

Benzo(b )fluoranthene 2013/04/30 

Benzo(k)fluoranthene 2013104/30 

Benzo(e )pyrene 2013/04/30 

Benzo(a )pyrene 2013/04/30 

Perylene 2013104/30 

lndeno(1 ,2,3-cd)pyrene 2013/04/30 

Dibenz(a,h )anthracene 2013/04/30 

Benzo(g,h,i)perylene 2013/04/30 

Coronene 2013/04/30 

Value %Recovery 

3.9 

82 

74 

83 

78 

90 

59 

82 

74 

57 

82 

59 

112 

71 

47 (2) 

105, EDL=0.81 

3.11, EDL=0.56 

<0.60, EDL=0.60 

<2.1, EDL=2.1 

<4.6, EDL=4.6 

0.76, EDL=0.40 

1.23, EDL=0.34 

<0.40, EDL=0.40 

<0.53, EDL=0.53 

<0.49, EDL=0.49 

<0.70, EDL=O.?O 

<0.76, EDL=0.76 

<0.46, EDL=0.46 

<0.76, EDL=0.76 

<0.53, EDL=0.53 

<0.76, EDL=0.76 

<0.67, EDL=0.67 

<0.38, EDL=0.38 

<0.68, EDL=0.68 

<0.39, EDL=0.39 

<3.2, EDL=3.2 

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

Units QC Limits 

% 5Q' 

% 50-150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50-150 

% 50-150 

% 50- 150 

% 50- 150 

% 50- 150 

% 50-150 

% 50- 150 

% 50-150 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

ng 

Spiked Blank: A blank matrix sample to which a known amount of the analyte, usually from a second source, has been added. Used to evaluate method 

accuracy. 

Method Blank: A blank matrix containing all reagents used in the analytical procedure. Used to identify laboratory contamination. 

Surrogate: A pure or isotopically labeled compound whose behavior mirrors the analytes of interest. Used to evaluate extraction efficiency. 

( 1 ) Recovery Exceeds method acceptance criteria 50%- 150% due to matrix background 

( 2) Recovery or RPD for this parameter is outside control limits. The overall quality control for this analysis meets acceptability criteria. 

Page 11 of12 

Ma•xam Analylics International COrporatiOn ola Max.xam Analytles f>740 C<rnpobei!O Roatl, M!SsiSSauga, Ontarlo,l5N 21..8 Tel: (905) 817·5700 Toll-Free: SOQ-563·6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma?§2-am 

Validation Signature Page 

Maxxam Job #: 6351259 

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

Owen Cosby, BSc.C. em, Supervisor, HRMS Services 

Maxxam has procedures in place to guard against improper nse 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 12 of 12 

Maxxam AnalyUcs lrnernatlonal corporation ora Mal<Xam Analytlas 6740 Campobello Road, Mlsslssauga, Ontario, L5N 21.8 Tel: (905) 817·5700 Toii·Free: SOIJ-563·6266 Fax: (905) 817·5777 www.maxxam.ca 
APPENDIXD 

FIELD DATA SHEETS 
\ 

TEST, Inc. Comments: 

_· -_··-f=-1--c~·· -"-1 --:::::-:;=--:- Sam piing Data , . 

Project W l ?~ () . Meter Box# ·,-polo %C02 --"''-+--

__ plant f.p [.,_,W". · ~eterCal. (Y1 ~ · .,:yoo2--'-""'~+-

Unit/Stack -Jtt ( /.U·' P1tot Cal. (Cp) ~; 3i . , ··¥;\rhco __ ~_· , 

Operator_1-*=ZfH·---- Nozzle# , ·~<-. )'?N2 ··· : 3 

Run# _ Nc;>zzle Dja. (in.) 1 •. ~ · Assumed Moist%· · · 4 

Date---'.3"'/-tS---.f....,l ].....---- ··stack Dia.(i,o.). · "·'- -- .. Final Moist.%---'--- 5 

Sample Time_l_lU ____ Statio Press.("Hg.) __ ..,e·Fin~i Isoklrij;ltic _% ~~ ·- \~:··· . ~ 

Min/pt c · Bar. Press; ("Hg) )_ ') .. 0; Initial Leak·Rate f1.(J(J ( ·Cfn1@ -..~f...:=O~_''I-;lg * ' 

Filter# Leak~-Qheck Vot Final Leak Rate.. . o -( cfm @ "Hg 

, Vacuu· 

Port/ Time Rate· m · 

' I.-

t;,}.~~~~~ ... ,.ot __ + 

: ~~ ...... 

i L-------~-~------~~--~~~--~~~--~--~~--~----~----~~--~ 

~~~ 

.-'. ' 

.i.,~.~.a~~;'}{¥~ii?J20;l.;~z~.--8>Jli' .. '·--~ · __ -~ .2L~.~~-. -f~ .:. ~.: -~-:~~~ }.~\,;,. ,!'· 

''_;";¥,~.', ' 
TES .. T I Comments: 3) ,9 'l '1 e /Q-,'7<..t"jj .... LJ 

, nc. 3 t6. 6i1 o e ~o~a ~.'-'1,., ;.3 

H <- ( Sampling Data il t:;' ,J 55 f1 9 D;_1750 ~ cl·'-1 

Project # I S'5 () . Meter Box # ao 1 D %C02 0. <f Imp. Initial 

Plant fc(.JW>./\ Meter Cal. (Y) J1 O~a3 %02 ¢0· s-' 1 

Unit/Stack· .~ "t- ·B H Pitot CaL (Cp} · .... 8<f %CO 2 

Operator J3X- · · Nozzle# %N2 3 

Run# "')... Nozzle Dia. (in.) [ ~ 5"" Assumed Moist% 4 

. · , Date =--i/t 1 { 1:J Stack Dia.(in.) . Final Moist.% 5 

Sample Time :---1-').. cJ · Static Press.("Hg.) Final Isokinetic% . ·~ · · 6 ' . -r- ----'-- .. ----· . Min/pt 5" Bar. Press. ("Hg) '1 ~.D.) Initial Leak Rate >00Ql ctln @ t 5 

.,Filter# Leak Check VoL Final Leak Ra'te l(jJ cfm @~: fD,.---.- H~g'---..... 

Dry Gas Pitot Orifice Vacuu. Filter lmp. Dry Gas 

l 

t 

.. . 

.:.;.: ... ~ 

f"··> 

."-Hg 

.... __ 

Port/ Meter (CF) · Velocity Press. m Temp. Temp. 

("H20) (F). In Out 
~. -T-EST Inc Comments:~. :;1. ~'l'fe 7"V w t;jt- ~ &..-3 .-~.. , , • . J £0. 6."' O@- '1JO *C(r~l-t '1..3 

(rl C I Sampling Data . .3 'i a 5 S" e 10 \ 'f t{V 1., Y 

Project# p, .. f )f'(} Meter Box# ;;) 0 10 1"'1 -?t %C02 D :5 Imp. 

Plant F-d"""c---. Meter Cal. (Y) c. o )0.2. %02 ,;;)ott 1 

Unit/Stack ~ {... A f-l Pitot Cal. (Cp) . "'5t--t %CO 2 

Operator C. -~ i{Y\ Nozzle # %N2 --~~ .. ~ ~------- ----- 3 

4 

5 

6 

Run# ~ Nozzle Dia. (in.) \ i ~ Assumed Moist% ~-7~~~--- ----- Dare___,3........._/1;..._.1~l..;_l_.3_____ Stack Dia.(in.) Final Moist.% ___ _ 

Sample Time-"'---\ J...-=---0_· __ Stat;c Press.("Hg.) Final Isokinetic% ·----- _ .... __ 

Min!pt __ (:::!,._______ Bar. Press. ("Hg) &'l.c')lnitial Leak Rate , oc \ cfm@ _\).. _____ "Hg 

Filter# Leak Check Vol. Final Leak Rate cfm@ "Hg 

Port/ 

Point 

5 ----...... 

'i 

I 

Dry Gas Pitot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

i :.:., o ._:; 7'~0 .t ')7 ("H20) ("H20) ( cfm) ("Hg.) (F) (F) (F) (F) In Out 

/~W1 5 t 5'7 ;~(;, a- . J. "kJ 5 7 ···-···-· ,.~ ·• -'--· ·--~ ___ .. _____ .. ,.,. .. _______ . . ·-·-···--·-····. --- ·- .... -~ . ..:----~ 

lro'SO 7r::::7,'t05 c,c:x:-JJ·-;- .1.0 ,'i51l.f -::s 1 'fi... J5b ;}5o ')tf 5't S"t 

;_, ________ ,j -:-~ .. ~ G -- . ·-· . .. ...... _____ ·---·-·· ----.. ------~-.. -----·-----·-:------;-----.l__;;:_; 

;). - (., \"ll'·) 7~3.'?l5"c_) o,uooS 1 ).6 SILf · 3 i \5::,- ~~"i:S !J7?/Ib7 5(;, 'S'::Z · 

5 \l)D '11Jl.CllS' 9,Gc:c6 ;}.C ,'zT/lf 3 \)b ,;}6() aY/ ~-'5'~ I'S"i J~ .. ~~ ; 

'-f ; l > <l 7 '1 ;j • 0'6 C' o, oocf1- ;}. {) • $?I~ ·3 iS' ·~ .? S 'i I J- 5o ~ <c, S-& 'S 3 ; ' ~----~~----4-~~~~~~~~--~~--~~--~~~~~--~~~~~-4~~-~ 

3 \l)e; 7'1b,;.24:5'io,oc:o'1- t?.c 1'-lllf 3 l'=-~ ..)$~ C>'-1<; '5'-i 'S'S' :rj 

_j 
TEST, Inc. Comme~D<.vs--~30 37 .JI5-e (,.D 

3s. 783 .e"--o 3 7. f3<J c_ 7o 01t...J,.,t_ 5 Sampling Data . f-lct e. . "e 80 

Project# ~ ,£~0 Meter Box# c20JQ %C02 0. 4 Imp. Initial 

Plant .Fe/.«u;q Meter Cal. (Y) 1. Qi)tB %02 QJCJ. 4 I 

Unit/Stack :P ~ f3/l Pitot Cal. (Cp) 0. 8'-j %CO 2 

Operator 13R Nozzle# %N2 3 

Run# 1 Nozzle Dia. (in.) /.'5" Assumed Moist% 4 

Date .... 2-dlo·/ J StackDia.(in.) Final Moist.% 5 

Sample Time dYo Static Press.("Hg.) Final Isokinetic% 6 

Min/pt /0/s- Bar. Press. ("Hg) .?f-/1-Initial Leak Rate .. QQ{ cfm@ 1'-1 "Hg 

Filter# L ak Ch k V 1 . I k fl @ I 'L /"CJ07 e ec o. Fma Lea Rate .CUI em "Hg 

Dry Gas Pi tot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter (CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point 9:ot) .2JJH "--olA ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

II· {p r.·os- ~'i'.J,bo.> lt.>. 0CK>5"' ).)- 8''1~ s.o 130 ;2'-/) ?$V [,() b& b'i 

w "1! lo ;)fr(p. J {)~ ·o .ol)c);;- _,d,:;J • :i'4¥ s-:o /.10 js-1 ~ ljf( b& ~9 &7 

s- 'i: /'\ .l-9a.~'1. ".0/Jl)'!] ~" • ¥4fi' :>-.n 131 .:J '50 ,;}SC-i 1117 7& 7tf 

j- 9~ .J.o ,;zl£.-8f!/ h.ooos- :z·~ 4848 .~b J39 as;;l ;~s-1 {g7 'il 8"0 

4 9.' ,;Js- J.tt;E3th.~ (),(Jl)O') ,2.:2 ~34'[) O:o t:=! 7 d'-Jto ,;J:ID (p?f 7d. 70 

'-1 9'! 30 .. -... ·."f'i-·:··~·'1,¥ 

3o3.1k~J o.~'l J.:l • 3"'18 S"Jo I ')',2 ~5:3 cJlti9 (p(p 70 (98 

. 'i ?.i 3.) 9o7 90J' oooo5 d..J - [1'q,<j t'5?0 J s-;;J JS:i ~SJ I.P8 7~ 77 

3 9/4o .JIJ.JQ) (),000>' ~-d 1- 8'4~ 6:6 Jt!./'l dSO cJ'SD s:r 7(f 7(/;. 

d 9!41) 3 J{., 70!5 io.o:Jo>' eJ.,) r8t/S '-5/D 14<3' ;;JSO 7~ ')J u) &3 

.:2 9/ :s'D 3-JLibl b. OW$"" 2.2 .6?/_'f5' S)O /0'3 ;?. ~1 ;)5?1 S3 &if &0 

J Y:ss- 3.,/5.' i.JD] :o. ooo>" ).J .?J<~r 5"L:i /39 ~ d_4Cj_ lib ur ~5 

I /tl! 00 3:<1. ~$ Oooo5 ).;) # 1i.Jf{ 0'.0 /39 dS7 t9'/9. Sl /t? ( ~% 

1/tltos- 3)'1. ~o:;-

/()- & /O~JO 33<{,/tJ8 D· OCX2'£ ,)..;) , ~tJ,f_ 5/0 139 ;}<J;). ,;1'-19 s-J 1#1 fpfp 

& !JOt 1.s- 3.18; 'loi o.Ooo$"' ._J.J .. fl'q}j S':D !'-/;} :?lS7 ;tsv fl'l m ~9> 

J i/DLdO 3'1:1/~3 ~-t:JcOs" 2.~ . "l?tt'f ,00 ,1/3 ~S/ d50 5l.J &<i ~aJ ~-OJ ~S' 34 7$/'0h lo.tJooS. ~:; .. .-W¥' 5/0 IL// ,;2'-j} ;l:)b .).J 71 7t) 

C/ IEtJf ":lb :J:rJHt>(p if).~ ~~J .3'kf' $)0 /~/) ;25'[) ;},,r;J .r;~ &7 &S 

'-l /0!35" 33"~ ~ /.rdt lo.o~ .J.J .fft./g" ,.:;: l) I 'IS" ~"JJ ~ID 5--uz- 71. .70 

3 10) 1./,f:J ~1 IJCJ" I oc.J lt'J.deoS .2::1 ,Y«-/{j' 57D /VO a-v9 .)s""D IT 7. 'j· .; .7t> 

3 /OJ 40: Jl#/.1/CB ~-~ )_.:J. • ~'l~ S' .. o /'II ~57 ~s?J J? 7:7 7/.\-:• 

:; llo!c_S'b .JG,jf. fjl)_s-" b.()ootr' .).J • 81.f8 r~0D /..._?'jJ ~47 :lvrr S1o 73 70 

7f7:<.;;)t)) ).;) 41148 / .;) IJt;!ss- p,OXJS 13}0 /'13 ~SO' ~5'0 tS7b 7ti 7:1 

I 11/Jbb J77.,qg 0.~ J.~ .¥W 5'~ Js-~ Ots-"1 ~rS'I s~ 70- 23' 

I 11/)0r' 3iH ,.t;dl ~. ()a)Yj! ;2.~ . 8'-lf ,~;, /'-/(; ~'-/7 dSI .5-7 7.) /? . I 

l i 

l I I i 

! i 

' 

-·~--------------- ---------- ----------~-·.....:.~-------- -----------

j 
Comments: 3 7, ;)/.)-c 60 

3 ~ -O(.QS"'e ::10 

:3 '5"" • ?'8.3 e 4.£. :J 7. cr .30 c:- 7o OJ wt.fc;Ls Sampling Data 3 (p ...tCi<l""" ~u 3 ~ &'liP e a"u 

TEST, Inc. 

Project# ~ 5TO Meter Box# (;;lo i o %C02 o. ~ Imp. Initial 

Plant hlrn6.L) Meter Cal. (Y) lw D;}.D3 %02 ,;?p.~ 1 

Unit/Stack.,.-7:1-: GJ. ·Bfi Pitot Cal. (Cp) D .. ~y. %CO __ _ 

Operator 1) 'K_ Nozzle# %N2 __ _ 

2 

3 

Run# Nozzle Dia. (in.} 1 rr Assumed Moist% __ _ 4 

Date Stack Dia.(in.) Final Moist. % 5 --- Sample Time Static Press.("Hg.) Final Isokinetic% --- 6 

:: ·· '· · . Miilf.pt Bar. Press. ("Hg) ;).9/ :r Initial Leak Rate."""C;....._,J+-1 _ cfm@. __,__..__--..,- tl.f 

i. 

I 

i 

i.~ 

i 

i 

~,~. 

Filter# Leak Check Vol. Final Leak Rate cfm@ 

Vacuu Stack :• ~-'·. 

Phrt! Rate m 

! • 

-:-,\' 

Final 

"Hg 

"Hg 

Dry Gas 

Temp. 

In Out 
I 

I 

~ . 

' 

I 

I 

i. 

i 

TEST, Inc. ___ (11\_d_.:,._l_S_ Sampling Data 

Comments: 3!. 06 & e .JO )s. )t 3 e ~.1u 

3 G I .. , c, q @ 'S (.) 

3/ , ?.. ,s- e 6 e) 

J},'1Jd€' )i) 

J Y. f:.t..ltol? fi d 

Project# 15 ! D %C02 6, >J Imp. 

Plant f ~. I,.._, CM 

Unit/Stack ¥ l IJW 

Operator (:<~fv\ 

Meter Box # 9 0 i V '01 "') iMeter Cal. (Y) t, 0 ~0 ~ %02 Q)o,'-i 1 

Pi tot Cal. (Cp) • "6 '-\. %CO 2' 

Nozzle# %N2 --- --- Run# '1... Nozzle Dia. (in.) --:---.....~---

Date ")/ 7.0/1] Stack Dia.(in.) __ _ 

Assumed Moist % --- Final Moist. % --- Sample Time ').."1 (.) Static Press.("Hg.) ____ Final Isokinetic% 

3 

4 

5 

6 ----------··-·-.. ·--- Minlpt toT~---- Bar. Press. ( "Hg) ,_.~ c; , I 5 Initial Leak Rate-\ o-co-- - cfm@ t ?- "Hg ---=--=:::--

Filter# J () 0 b Leak Check VoL Final Leak Rate 0 cfm@ tO ·"Hg 

Dry Gas· Pitot Orifice Vacuu Stack Probe Filter Imp. Dry Gas 

Port/ Time Meter(CF) Velocity Press. Rate m Temp. Temp. Temp. Temp. Temp. 

Point oqoo "B~ t."~C)?- ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

it (a OC.' o"S f;'(Jb.,Oj~ o.ooo~ &.o ,i>\'1 Lt.o t"SI -~ '5b P'-'-l 't <;;," L(~ '11 

0 O"'LO ~~'1. C,'15 o.o:ctFi 'd-\0 ~.:f>Vi Lr,o t-s-5' f.J5i; ;,).'-(! '161 415 ~.-,<; 

.:- t:>~ 15 I) "g'<=i.1,'1<i () o.occ":> d-,0 .-<3 i.t.' t.t,n l5~ .;1{;' J~-( ~j- S'S"" 'SO 

~ oet.?c ~or:g1ob'S D~Co05 'J-,0 .~tL( i-(,D 'l "$ q_ ,)6"'3 3-'50 ~ :..( ")) S"'\ 

t-t 0'"\ ;}") . (t 0?· I"' 0 o.(X)O') ;),0 -~Lt.( /.tJ) \)6 Jft.j-l o4'1 "s- 'SS ~0 i----·----,· ······ ······--·-- 1--~·-··- : 

t.r cr{aD q {)(-,I) 5) . O,t)(.(.J ') ;;).0 I ~l t.( ' "1,,0 : ;;.")~ ~~~ ' \.') '-{ :2So ~:I. ''-!~ ...... - -----··-- +-- - , ... _. ~ 

·~··-~ 

~ 0"\ '35 4&0,·~~0 o.ot::OT d•O ,1<\4 i-1.0 \ '5"11 ;?51 ~"50 <e-2 ~1 lt'l 'I c9tio '1 \<-t,)a? o,ex::o<J ) ;),fJ t'OIA1 -t.o t') \ ){;,') :JJ.SI (,D 'il -'(<"\ 

2 Ol:JI-1'5" 'i I 'iL S"i S" c.cc~:<:J :).0 .~\1.\ Vf\D i:5"2 tP-55 ;;J.~ .. , {,O ; '-$~ l.f~ ---· .. . -·· - ... --- ~-- ''o ..... .... ·-----

') O''t50 O..)~.lO[ o.ow'i d·D . (!Vi '1.0 l'S'~ ~·)"3 &-so 'Sl '1'\ 

I (71 '}'5 ~ ;i}b, '7.3 t"S o,c;oc/) ·d· 0 1'8\tt 'i,o lb() a?1 ~-5'2 ht $1 5o 

I IDDD '1. ~o~<;,S"7 ChCoiY) d,O ,'di~ Lt,O I b \ dfo2 &S<."'l (,l "5".1. 'S~<) 

I oo '$' 

. i:$~:f;~J,· '1 ~ '5, t)~ (ill o ,caY)- L~t"i ; 

L;;tL_ 1.{,1 ;)51 . ~s-o b'S"" )~ ~9 " !DiO (i).D 

::;<;?'~~0 I o t ':1 ut~Cf.i). 15 o.c< {>S ;),-a ,1\"\ t.{. c I C::. o ;;56 #50 b1 5~1 lf'l 

i 

:-'• 

;;5'5' . .:;.s-. so! ... , '5 (o;.C .-,,J.,~ ,-'100 O,t.:J(I('; ;),b .~,~ 1-(' c t (;, J dS"O (oO ;~-~- -, 

·s-.: lu:t~ '1 Ll( 1 L(~.; 0. cuo•) d·L ,'?>II{ "1.'D l)b .);~I ,;)~, -;)<\ s~s ')O 

Lt . rofo .:t "5 I ,") '50 o,oro) lti-0 ~~Itt t..,,o ~~() C>bS ~'50 ~q_ '51 '5D 

·t.r I o,:; 5" "\S''),!..f,O {), c-c:r.>5 ;).o .~\4 l-{,D \oS l r53 a-'5 I 'S"1? $7 s-o 

) i o<t D q~9.T?D In .c>Orfi ~.o I '\S\1.\ '1.0 l-5'3 }j"~ J-50 .. -" '5"':>~ i ;) tt1 f-----· ---·-···· .... . -~~ 

' ~-··- ······-·-

.3 ' i 0"()- ·G61:~ZO eo.oot:) ;>,0 .'6l~ 'Lt,O I '55 1 )5"1 )')() 60 '-5"E, ~s-o 

J I c "5 '-' ~b<l.d10 ! {"}t cr_(, ·:- -;),0 1~\Ll '1 .. 0 i5~ ;l-5<1. .J.·5o 1'\ ~1 sc 

2- 1 c':> ,. C)1dl t~'S v.ooot:; d-·0 .<gt t..f ""I,() I S''f _J6( diO b l -s-g Sl 

I /li.IL- q1b,1~0 o.cr.</J' . ;).~ 0 /6L't ,, .o iSf. .).G.:) I Ol-'?D ~'-1 ~)6 56 

:'1 ~ .-3 <1 s- : ''... ! ;_-D-- I -

t t l o) ~~~e-~. 1-t,O i '5 b ! )~1 :2~ .b'5" C), . -- t C. t•D[ :J • , 'Sb ~i 

t ll 0 I 

' ;:;_ (, tl \) ic; ~I• "5 iS'() 8),()00~ J·D ,1S\l.f i.t, D t '5" e 0H, l Jc;O (,1 "5"'{ lt'l 

6 h.?o jtt-g-g.l0() ln. ow 5 ;),0 /6i~ ~0 15'3 t)bO ,;)5f 63 SJ .!fcl 

i 

I 

I 

j 

l 
'~ ... 

\ 

TEST' Inc. ~Comments: 

-----'M'---'-"e.;.....;.-t..:....;v'_,_b"-· ___ Sampling Data _ 

Project # t '5 S D Meter Box # . 1 o 1 o Y'"i ~ + %C02 o, E.( Imp. Initial Final 

Plant 1:.;. l ,..,.,-:;,(\ Meter Cal. (Y) 'L o) c 2 %02 )C, (( 1 

Unit/Stack .t> )- J) \:-\- Pitot Cal. ( Cp) , i ~l %CO 2 --- Operator L -'1) f'\ Nozzle # __ _ %N2 3 --- Run# ;j f\ -"'--'-------- Nozzle Dia. (in.) L. ") Assumed Moist% 4 

Date 3 · 3 C ·· t'} Stack Dia.(in.) Final Moist.% 5 

Sample Time ;~.1-! 1) Static Press.("Hg.) Final Isokinetic% 6 

Min/pt ,_..>;....t_C....... ~~ t:f-. ---- Bar. Press. ("Hg) -.)-.. -"-· -1 ')-.. Initial Leak'Rate cfm @ "Hg 

. ~ ...... · .. 

Filter# 

Port/ 

Point 

') ' 

"-{ 

'1 

J 

) 

--- i oo £-, Leak Check Vol. Final Leak Rate cfm @ "Hg 

Dry Gas Pitot Orifice 

Time Meter (CF) Velocity Press. 

'\ '5:6. 7 !U.~ ("H20) ("H20) 

lC..(1 ( ,,i::j D:Ct'\:'·,-

I \ <j ·r 1 c··r, 7/-r..) \ ' "' • .;;.. C• --r./( 

iu-)l:.,i )' C o.c.:-o .. /,-

-- c .. £....:6,.-') 

104/' ()~0 J.o 

C..['f.>l.') 

Rate 

(cfm) 

I~· 1'(' 

Vacuu 

m 

("Hg.) 

~;.0 

.:.( .ZJ 

i-{, 0 

"'{.0 

J-1,0 

,_,. (.1 

·--: ~ c·. 

Stack 

Temp. 

(F) 

{50 

I '5 .2 

1'52 

tYc; 

l'SO 

I'$" \ 

Probe 

Temp. 

(F) 

Filter 

Temp. 

(F) 

.,'\. 

(7- \ 

Imp. 

Temp. 

(F) 

Dry Gas 

Temp. 

In Out 

5; so 
", ::~:;;:~E S'l1;~i In c.. ·. -.. . , ... :_, -·~ :c,(~/tfc:,_(S -<';~:., S~mpling Data 

Projec~~# · . ·.c.f{l?;"'>·,~i_·:-. :.', Meter Box# 

Plant f d-IM..~ .-;;~4'~,~t':t,,, , Meter Cal. (Y) 

Unit/Stack. -~ l- AH . · · :'i'~~~~,::~·Pitot Cal. (Cp) 

Comments: 3_;-, 0 C. fl ~ 0 J) ,·u 5" 

:15. 1 ~ J t..l 0 3 '). '1 1° 

: •, . ;,1'·4 '"'11 ~ ; 0 3 t. '"' (., 

6to \ o ~ %C02 0 ·, e:../ Imp. 

\ •DJ 0) %02 ;::)Q,~ I 

~1/J. %CO 2 

· Ope~ator C5. (\'\ · , ·,_ ·. · :}<;f,.':;:. Nozzle#· %N2 3 

Run# 3. Nq?;l;I¢~:Dia. (in.)-1-, -5- Assumed Moist% 

, . Date 3{1-0/IJ Sta~~f?-~~;\fn.) Finall'yloist. %---

--- 4 

5 

:,_;'sample T-i~e 't ~~-\ D Static Pre~s.(~'Hg.) Final Isokinetic% 6 

Min/pt flJ f( BaL Press. ('1Bg) 1 .. ~.0S Initial Leak Rate_;,;.=.""'--=--

. Leak Check Vol. Final Leak Rate :,· . 

·orifice Vacuu Stack 
. ·' 

.. liP'-~, ·.'\~~-·.;z·.: .. . ' ~ ........... ..::.: ...• , .~.. . . . 
, ,.-'IEST, Inc. . . . . 

:·:,·! (J; ot. 1~ / ( '4"'--"" )Sampling Data 

i .. 

,,. . P~oject # f I i" ( {) Meter Box# &otD t...._¢ %C02 Imp. 

Plant (- e t"' C>\"' MeterC~L (Y) t, 03tr].. 1 

Unit/Stack -1:1 ( 11H ' ' P·it~t C~I.(Cp) , 1/1 

%02 

%CO 2 

Operator C.?>JM. Nozzle # ; ----:----~ 

Run# l Nozzle Dia. (in.) \ · • ~ ~Assumed Moist% 

3 

4 

%N2 

Date 3 /1 1 / r j Stack Dia.(in.) ··~ Final Moist. %--- 5 

Sample Time l 'A e) .. Static Press.("Hg.) . . , Final Isokinetic% 

Min/pt ;- Bar. Press. (''Hg) ·~·<?.d( Initial Leak Rate __ _ 

6 

~ .l 

1 I 

Filter# Leak Check VoL Final Leak Rate 

• ' ... i I 

Dry Gas Pitot Orifice 

Port/ Time Meter (CF) Press. 1-----t--"'----~ 

Velocity 

Point lm'S~ 

7 0'10') 

b 04t0 

'5'· ~9lS" 

'-/ e)"\)0 

"3 loq).s-

·.··2~·;· 09'3D .· .. 

09}5 . . . . 1 . 

!IO{L _.,i:' • .-- •• 

r-531·~1s- ("H20) ("H20) 

<S~<S" 'los- O.cco{ (;),Q 

St.tf)LD(j)S" 0 ,001;:)~ ;).,Q 

")'{'"( Ol') olooo$' ~,0 

-s~\'t> .• \l$" IOtOct?'$' .).O 

'S 5;i,l )')(!} ,' 

tJ .. OCCI':)- ~,0 

I S5' C:n J..f 7 D 'o 1 Dc:05" d·o 

s &-·o, ·i;'l s- lo,occfi ;??,o 

if. 1-J ,(V () 0 OOD) ()-0 

b ~;?, 'J J (? 0; ()(){Y) 

(,;)6c5/') ()i.OOQ'J ~\.0 · 

' Vacuu Stack Probe Filter Imp. 

Rate m Temp. Teinp. Temp. Temp. 

(cfm) ("Hg.) (F) .. (F) (F) (F)'. 

;"bl~ '5 iSl db.2 ,?()2 'S'i 

1~\\{ ·'5" 1.'f7 d<00 pll.f~ -'-i( 

,t:6t}1 ~ (~~ /)-bJ ·;;>.Lf4 t.f') 

.«&\"t '£' t~O ;)~? ;;>5:2. LIJ 

l"ifl'1 5" tG:.C:. J"S~ 8-')0 5"2. 

• "gl Lf. ~- ' j(,. ~ ';,.~L\ d.-'5 I S""':> 

,i\J.f ''S 1f.o~ Jb ( tl-5'l ·r-s- .~I¥ ~ .,. . l <:. I !){;0 .?SI "SJ. 

,"8/lt S \S~ 'J.S'-6 Jli€) .:Sro 

1s- ~ ·a.-s1 1.1-so 1 -~(;;, 

\ ~ t ;;;i:,,o_ .' ?"5" 1 ' -sa 

"Hg 

"Hg 

Dry Gas 

Temp. 

In Out 

"S;. '5"0 

"'S't( 5"( 

5<-t 51 

~". S:J 

~() S.:l 

':":\) 5 .2_ I 

ss- h'2 

~.;l. "So 

\ ·--!-----;-,..,--+--, 

I 

.I 
TEST I Comments: 'l( .'1-<t.i' g SO -... , nc. !' 

3 ) • 2-oO, @ 6 0 '· 

(J I u>c.·-'\ /fv/'OpAJ Sampling Data ·-~~ ) l; '14 l!.. ) 0 Project~ :h{;- l ~j() Meter Box #L-a-.. -0-\,'-"--0-~--_:,."t:l=-· '_,_t"...:.....:~o/!-=-oC.::..0--2L::::t.:_L)_· -\t{-:-------_::__ __ ___j 

Plant H ~-~' Meter Cal. (Y) \ ... t:'~o2... %02 ao\-5 

Unit/Stack $(7 \b\-t" Pitot CaL(Cp) ~ '8 '-! %CO __ _ 

Operator c__IP \'Y\ Nozzle# --- ~ Run# 2 Nozzle Dia. (in.) 

Date ] pe., ftJ Stack Dia.(in.)-1-. -=(,--

Sample Time \ 10 Static Press.("Hg.) __ =-

Min/pt S' Bar. Press. ("Hg) 1 ~ .o-'i" 

Filter# Leald:heck Vol 

Port/· 

Point 

Time 

'\ ')_.') 0 

\J.~'i" 

Dry Gas 

Meter (CF) 

e:, "5 '), zg,o 

ra"5b3e,_S" 

t:,.LtO:!>c;(! 

{:8i" 4//0 

c·t3,S'""""?Io 

Pitot Orifice 

Velocity Press. 

("H20) ("820) 

O.oao ( _d,6 

t-\-ccoS" 9·0 

0,0()()) g.o 

• o.mo'S ;),p 

Rate 

(cfm) 

%N2 

Assumed Moist % 

Final Moist. % 

Final Isokinetic % 

Initial Leak Rate ,00\ 

F ina! Leak Rare • au I - Vacuu Stack Probe 

m Temp. Temp. 

("Hg.) (F) (F) 

'5 l ~'\ 016~ 

;,) t '-{ '3 J>t;.9. 

s I t..l '\ ~~lS 

'S" \Sb ;y5t. 

"""' ;) t-51 ;)~'-1 

'jg;~\i:':t,.. l)oO t,(:,I,OO') t>•bOO~ :;:L.i> cfb\~ l{"" /"15 ;):<., j .?4~ t..-('7 ~J. LJ~ 

~~-::~~ ~ ·L , np~_ ~b5 .. ~~l?-!L-,9295 , .;).o _ t'"btl.( ___ s- "'<;_ J.il_,.2,io _2.~--~-:--4-~~------~2.-,-'5"'u __ ! 

.. 'i : l) I O : (,(:.~ 1 jr;~- 'o ,ceo') ,), 0 .'311.( "!) ., <-jL.j d $</ ' fJ5D i l-(.<:(, , f)- 'y() ; 

··.~· 3 ntS"' bl3':s;o o.OCD'5 ;;,e> -1\l.f s- 1'1~ ;;<;b ;;1c:.1~ '17 st t.t1' .· .. ~ . 

.. ··r 2 (3 J'D to"?/, {OO OdJOO') d-D ,'f>ilf %;" f$""0 J'S~ ;;)5 \ _.<.\q -5/ l.(<q 

.:/ I i);:.t-)'- b<&i.-~J.ts· o,ooo'f ;;;,o ;'6i~ ) t5J J~l ~4'1 5a 7/t tt9 

I ' - t )"3 0 t ; . ' I ! ' ... :,· · i 

j·ct. - [, b 35 ~ ll~. c 0 ~ c.~-r;:;; : t~ t~t.;J ) llSJ1 J 5"1 . ;m 1li'l'""'F+ 5-o--t-t.t-'1-1 

.~, .. · "·•·' '' .:-:S __ L!.)_j_()J~J-~-~~_?) /'·ooo5 !. ?:~ ... :.)_~Lii~ ...... ' _ _?. _____ _Ll~ 0 __ .L~!J __ !_ ~-~<?.L "~ So 'i~ I 

' - t-;'-;-·.. t!/1_ .· 'iL?,_t5 'l:.9'3 .Y1 0 ;o v0c,s- . d-':o .~ \ '1 S i 'S" D , J 59 ;)50 D 0 -;)) t ii I 

r r-J'So £91.~-'~s- o.cod) ;;,o t~\~ s- i ~~ 1 J->5 ;;~~n cs- :;J ~-~ 4q 

. ·~ . . : ' 

I t'l:.tDo \vtt,l\6 0 .ooo'f d-.v ,?JI'-/ s- ''-t<., ILl(, :>57 ;;5o 1.2 --)o · 4q. ·;---.. ---.. -- ._ .. ____ ... , ..... ---- ~----- ....... ;----~ ---- ~--:-·--- :··-----·T-i 

i/,.l05. 

b /~I[; 

5 jL-ji':) 

t-r }t.JJD 

3 I 'iJ) 

/... lt.t3D 

I lLf 3'5 

l 

1 
·-: 

I 

Comments: 
'""( f'• 

TEST Inc Comments:~~" ./ , ' • ") .J • Q ._.,<( £.. Lil) 

~ . 3ue 54~C~ -----4~'-~.!:....!.d~'}\ ___ Sampling Data , 7 ., "'t e.&· 

Project# J <05/) Meter Box# ~0 t·O v'I'Vi) 1" %C02 Imp. Initial 

Plant ~-c{mc."' Met~r Cal. (Y) \ J:':?~ 02 %02 1 

Unit/Stack '#- d: BH- Pitot Cal. (Cp) /.)"'~ %CO 2 

Operator \3 R Nozzle# %N2 3 

Run# \ Nozzle Dia. (in.) 1. ~If Assumed Moist% 4 

Date 3 -;8'-1::\ Stack Dia.(in.) Final Moist.% 5 

Sarnple Time _ __,,,_/ ail-:---·-··· Static Press.("Hg.) ____ Final Isokinetic %_····-···· fi ······-···-···---

Min/pt .;:L Bar. Press. ("Hg) ;)[f,qc;- Initial Leak Rate 0 ctrn \ .2. "Hg ·-- Filter# Leak Check Vol. Final Leak Rate .. <.90:1. Cfm@ \ !2_ . "Hg 

Port/ 

Oriftce 

Press. 

("H20) 

Rate 

Filter lmp. 

Temp. Temp. 

(F) 

Dry Gas 

Temp. 

~ ~ _· ~~.,1--+----'--f----+-----l· 

t~ ...... ~,~~-~~~~~ 

-----~ ...... ----~----------- .• 1 
' ri 

t ·' 

TEST. Inc Comments: l ~- ~b { e 4 () :~t ,<J I) e 70 ]\'' 0 

JfJilfrl ~6. 5~t.e 'Jo ___ n-----'----::-=- Sam piing Data 3 1 c; @ t;, 0 

Project# i'S"-60 MeterBox#$?D{O~t" %C02 O.,j Imp. 

Plant f. e.\~(\ Meter Cal. (Y) · h0)02.t %02 ~D;t{ 1 

) Unit/Stack ~-S~ \\; Pitot Cal. (Cp) _ , t'j_ %CO 

Operator ~ \<\ Nozzle # %N2 ---

\ 

,, 

2 

3 

Run# C, Nozzle Dia. (in.) ~.L_-Assumed Moist% 

Date 1-1~ .... , ·~ Stack Dia.(in.) Final Moist.%--- 5 

Sample Tirr1e ___ _!_,2:_9 __________ Static Press.("Hg.)- . Final fsokinetic% (i 

Minipt ~ Bar. Press. ("Hg)·1~5- - lnitial Leak Rate a-D?\ c1in@ __ t! -- ..... ,;Hg 

Filter# Leak Check Vol. Finai Leak Rate ., 00 ~@ 1 "Hg 

Orifice Vacuu filter Imp. -~ 

Dry Gas 

Port/ Time Press. Rate m 

Point 

s- 1 

1 

&, 

"( 

~ 

E 

I 1 d-~D- l6l~¥.C!.2'_Q,()oo<J_ I /7 ~ i:_g ____ Z:CJ i /7() t- :?::?- ) J(p I .4 0.1 ' I I 

~ lj LJ3D 3W¥'4J I) .. (Ja>··i ,7~Lt Lt( Zo 1&:? 

____ 1 ~ ~- s-~ ~£ 7tJ& I 4~RJJ_t?._y: 1 .7~t:.. _f-:'!l '.o lz //;7 I 

b d-_4 {) 3_ 71)--; SlJ;J. ('). {Jt;r)L/' .... 7~ /. C( I _z.Q_ l l_(/7{ 

1\ ;)i.j) 3$'0 .,JOCf b~otJCf-1 191/ ~9 7vt') ltw0 

'1. ~'5() J 1'1. 9&1 0·0DD4 ~ 794- /~C't- 7--0 /(;,)' 

J ;;;s-s- ~<..5 31. (1} I [). {)l:JlJt.f ,7'7~ l- Cj_ 7"'o /(/J( 

:J, aoo 3W90) · (J,CJUtfll /Cit? /. 7 /,a 1&9 

- I ~ ~_$_Qj__LQ,tvD4 111qfR 1.~ -zo /&7 ---··--1~·---~·-·r---

,... ·J .. i I 

! 

i I 

Temp. 

In 

';z_d:>/ ~'19 1bt5 (fl idv 

~ ~ ~ -~ ~--

.;::?-.5? dJs?> (p~ /) ff 

.,;J ss- : ;/.-!>0 &3 ll:?i:_ fr<.iJ I - ~ ·-.. --··-- ··-··-- (jv--· .7;r ! l(p ' '_;J,S(.... ;;s-o 

d'J'fj _;;s-o fp;( 78" 77 

~r id-51 ut 7&7 "hld1t,l> ~3:2 ft;<-{ 7T 7& 

';}/;l) ;)-49 5r Z.p- I~ 

;75 · 4VCf s-s- 7?r ~~ 

j 

I 

I 

\I 
I 

r 

I 

TEST·, Inc. Comments: 1'1/,ot 1 @ 7C 'io, \b<i' ~ J<'~a 

0 .A,iJ.. )'/? 7'31-1 @ '$O __ .___;.h_Vl.:....;,_· ___ Sampling Data 1-=t' ""t'n e 'iO 

Project# \ ?10 Meter Box# 1).0\.b VVt"a<t' .%C02 o. '1 Imp. 

Plant <IF-c...l~~""-"""' Meter Cal. (Y) \ ttD1D1- %02 ;u:>,:f' 1 

Unit/Stack ·~ 2. \>1\lt #~1·e Pitot Cal. (Cp) t j "f %CO 2 

operator ··e.~· V'\ · Nozzle # %N2 --- 3 

4 --- Run# f3 Nozzle Dia. (in.) k') ------ Assumed Moist % 

Date _..::,___:..!f--;..=--. ~ -l'8'-t'3 __ Stack Dia.(in.) Final Moist. % 5 --- Static Press.("Hg.) Final Is<..~kinetic % 6 -- ---····-····. -·-· Sample Time ____.\~9--=o"'-· ----· 

Min!pt {) --"----- Bar. Press. ("Hg) 9'8 tl'f" Initial leak Rate 1 00 \ ct m .( -t g.. ·· H1:0 

Filter# 

Port/ 

Point 

Time 

Leak Check Vol. 

Orifice~ 

Press. 

Final Leak Rate 1()0 ( cfm@ ft./. 

Vacuu Stack 

"Hg 

:Dry Gas 

Temp. 

In Out 
_.c·· 

EX 

Sorbent Trap 

Chain of Custody 

Test Location: .' - ~ \t_) ~- '- \ 

Trap ID: OL /5 b-0 3 Lj 

Trap W B (Circle One) 

[ZJ Unspiked D SpikedAt: 

. ~-~ . 

Certified Accuracy± 10%, Traceable to NIST 

QA/QC Signature ,T,,.M,.~ 

Spike Date: ___ _ Spike Time: ___ _ QAJQC Signature (Spiker) ------------------- 0 High Flow 0 COIL 

Estimated Hg in Section 1 :----~-----=n.::.-g;o_ 0 Static Prefilter 0 AGS 

I8J.185 mm 

0240mm 

0300mm 

0450mm 

Sampled By: (~ ~.> f'v \. 

Test Start ) /1 S /1 ) 

Date/Time: 

Date Time ~r·mp F roC) 

~In- )>, ;;~ i~-3 

11117. (51 

'bl \'14 (\ 

\~ i ,;10<;~ \ 

·:>_ .' \ -~ Q, 

-' I i 4, I ,":J ::r;; \ 

'. " •I: lb"i' -'I "' "h ~~Co(') \ . ~' 

'3i 1 ~o11 no I - ,.,L_ 'v r 3 ~:17. 1'1\ 

j Total/Average 

Sorbent 

~Temp Or°C) 

;t~ t 

_.).K.< .. -· "~/') 

tJ '-

& < .- \ 

':.f..._) 

,')~ L 

~~ .. ~~~ 

;;.<;o 

Type ofTrap:. ___ ...::3....:0~6:..._ ___ _ 

Test End ~- ;~?-: -:;. 

Date/Time 

FlfJnRate Dry Gas Meter Dry Gas Meter 

{!f-_cj in) Liters Initial Liters Final 

Lt. oc c,1(..;00 .c.; J(IC' 

"iCC "5 I~(:'(~ 1~:~4'5 ~ - ./ :J "-·i . -,(::, ( ', ~i,.o~::: I. k;. /-(-::, ":- £# i I ;.'r '\._' 

·-/ n-J t_ ... (_..., 

~ '-i 'v2J·;;_;.\ ;;/ 1 :.; \ -~~:~ .::, 

., '. ~ -, i "--'. ·:-- --~ .:.~ 

'-t_C,J(_j ~J ::::-- ... } -

t.t.uO •t t ' '11") )U,( ' I ( 

<--j "DO ·ri:•, tT7 

heck,.~ p ··.ail e_.;~ 3 

Total Volume 

Pulled 

1")0, (17 

Chain of Custody 

. , ''.Relinquished by Tech.:.---l....(2..£.k~!:...~~:..:::"")~£:.....:(Yl=----~cz<...[...· ~C..c.'d-=--~?j} __________ _ J..l ~ J - l "l Date: ' t t ..J --------~~----

Received by:. ___________________________________________________ _ Date: ______________ _ 

Relinquished by:. ________________________________________________ _ Date: ----------------

Received for Laboratory by: Date: 

Make sure all of your sampling conditions prevent moisture condensation in the trap media. Moisture condensation is a major cause of breakthrough and spike 

loss in sorbent traps and should be prevented at all costs. 

For Analysis contact us: 

Ohio Lumex Co., Inc. 9263 Ravenna Road Unit A-3, Twinsburg, OH 44g87 USA 

Phone 330-405-0837 Fax 330-405-0847 US Toll Free: 888-876-2611 

Impregnated Activated Carbon- Refer to MSDS 

Deactivated glass and glass wool 
EX 

Sorbent Trap 

Chain of Custody 

Plant/Source: f~ ~ I, , ·--<, f' /)3-if ~~~~L-~~~,~~~----------

Boiler ID: M: .? l 1' t1 ··\ \--- ~ ~ _,_ __ ---------·~··-~~~~-~-·~-·'~~--·-'-~~~------­ ......... ) 

IZJ U nspiked D Spiked At: 

Certified Accuracy± I 0%, Traceable to NIST 

Spike Date: ___ _ Spike Time: ___ _ 

Estimated Hg in Section 1 : ______ __:n:.:;:g::;t.. 

Sampled By: __ e_=.,/.....;:. :;;::::....._(_1,../1...;/:..... ------

Test Start :ft/ I~; (I) 

Date/Time: ·--=--- ... -~ 

,_} 

Test Location: C. c- /l yc (: \:'l 1 -::· I· .-

Trap ID: OL . / 5 6 D S g 

Trap A ~ (Circle One) -· ~ 

QA/QC Signature (Trap Maker~A-4...------

QA/QC Signature (Spiker) -------------------- 0 High Flow D COIL 

0 Static Prefilter 0 AGS 

181.185 mm 

0240mm 

0300mm 

0450mm 

Type ofTrap: ___ .....;;3_0~6;;;...._ ____ _ 

Test End ·1- ~--j · i "?; 

Date/Time \ ~. ~ ;;>-~ 

Date Time q~tTemp 

(D:/or 0C) 

Sorbent 

TE',PTemp 

('F)or°C) 

F~~ate 

~m) 

Dry Gas Meter 

Liters Initial 

Dry Gas Meter 

Liters Final 

Total Volume 

Pulled 

.0 .• 000 

·7-S',-;.::) 

')! \ :::~.2~- 1-.::: '-'· ·~ - • tL- -

.j~'\ J'j ,,) 

_. \. ~ or ' I 

I Total/Average 

... - - '·-

'i, ~2C> 

':1-o, 56.? 

Chaip of Custody 

Relinquished by Tech.:.-"'~~ 1 ::..!:· ...:!...!..</,:_ctX~··~~,...L)__,S6"'"· L...:._fV'k __ .:=:::::;~~i..""'vdJJ"'--"'~~.=-------------------- Date: _-'---=.t'--. ----=-r_-_l__:3'-----

Date: ------------- Received by:. ____________________________________________ _ 

Date: ------------ Relinquished by:. _______________________________________ _ 

Received for Laboratory by: Date: 

Make sure all of your sampling conditions prevent moisture condensation in the trap media. Moisture condensation is a major cause of breakthrough and spike 

loss in sorbent traps and should be prevented at all costs. 

For Analysis contact us: 

Ohio Lumex Co., Inc. 9263 Ravenna Road Unit A-3, Twinsburg, OH 44087 USA 

Phone 330-405-0837 Fax 330-405-0847 US Toll Free: 888-876-2611 

Impregnated Activated Carbon - Refer to MSDS 

Deactivated glass and glass wool 
Sorbent Trap 

Chain of Custody 

T t L t. r; .. /"• 1. r·· \"· t' es oca Ion: , __ c v ~_,,: ( , , _LJ ~ }::-·-

Trap!D: itJ. /SGO 6 CZ 

Trap _ B (Circle One) 

IZI U nspiked D SpikedAt: 

Certified Accuracy± 10%, Traceable to NlST 

QA/QC Signature (TrapMaker~ 

Spike Date: ___ _ Spike Time: ___ _ QA/QC Signature (Spiker) ________ _ 

Estimated Hg in Section 1 : ______ ---=n=g~ 

0 High Flow 0 COIL 

0 Static Prefilter 0 AGS 

I8Jl85 mm 

0240mm 

0300mm 

0450mm 

Sampled By: __ C_-u_; _("'_"'\. _______ _ Type ofTrap: ____ 3_0.......;..~~-----

Test Start 3 -l ") · t 3 Leak Check 0 

Date/Time : r~ ·, 5 -:J 

Date Time ~Temp Sorbent 

roC) ~~emp r°C) 

3[ .:;, t 3 ~·-;- ·~ l ~s t I " 

I. ~ l.t4 (.:;: ibO :J-50 

3/(< ... ~< f.'~./, 160 ;;50 ') 

3ir1. 1'1') ")- ; / "/ t =..-- .:) < ·'l ..-'-" 

j' ~~ (? ,.:..· J • j ! "0 ; "-{ '1 

;')3~ t<,G,. ;;. -:) D 

'

1iti t:\'5:) l (c.-:, ._. d-5c> 

j Total/Average 

Test End :. ~ ~--:; · ~ J 

Date/Time i 'J ·. :.; <-:.:-

Flow Rate Dry Gas Meter Dry Gas Meter 

@tin) Liters Initial Liters Final 

"-"f.CJ 0 it) .ooo 1?.,"7;:\G 

t.tC'O ..c;:.. ~ \r~ 17 ;,.:·o 

400 ( (.j'50 ;?. <;. \ ~ 3() 

tr DO a:)~\ ~3c )'-r I :.r '"· I-:...,. -:x 

·-

1?;; :1 •;, '10{) 37.~'1'Sj ._, J 

?.l f)C) 1 )' :;- -', I •- 'ij .;. . -· ~ ... · 

-::c·oo :.~~ '~-~-·.) 

Chain of Custody 

Total Volume 

Pulled 

.·, 1 I .. ;.:2 ·1''{"l ~ IJ f/ Relinquished by Tech.:._~\._.c<:._'_"':...:' C"_··:::.._A_ ..,_,,._; . ....C·\.._!J ___ ~·~-/-'\t.=-' c·_,\. . ._,f~Y __________ _ Date: _!._i_·_l _-·-'---::.._~---

Received by:. __________________________ _ Date: _______ _ 

Relinquished by:. ________________________ _ Date: _______ _ 

Received for Laboratory by: Date: 

Make sure all of your sampling conditions prevent moisture condensation in the trap media. Moisture condensation is a major cause of breakthrough and spike 

loss in sorbent traps and should be prevented at all costs. 

For Analysis contact us: 

Ohio Lumex Co., Inc. 9263 Ravenna Road Unit A"'3, Twinsburg, OH 44087 USA 

Phone 330-405-0837 Fax 330-405-0847 US Toll Free: 888-876-2611 

Impregnated Activated Carbon- Refer to MSDS 

Deactivated glass and glass wool 
WI EX 

Sorbent Trap 

Chain of Custody 

T L . ,.· \""-.}"#I est ocatwn: , .:: .-\ ~ r.:. I< •--'·--· _. --~----~----~-----------

Boiler ID: b.,~:.> :0 t-t --~----~~-------------------

leto NIST 

Spike Date: 2.//'-I//3Spike Time: /'-//0 ~--- ~ 

-·~'liF 

QAIQC Signature (Spiker)-~~:::::::?::: 

0 High Flow 0 COIL 0240rnm 

0300 mrn 

0450 mrn 

- Estimated Hg in Section 1 : ______ __;;;n=g""'" 0 Static Pret11ter 0 AGS 

Sampled By: C "~ (Y') 

Test Start -~ 1 ,"'-3{ 1 ~~ 

Date/Time : \ j \ •-) :; 

Leak Check .::;; 

~/Fail <Jt_;_ ~ 

Date Time Duct Temp Sorbent 

(°F or 0C) Trap Temp 

eF or 0C) 

'"'-: . 1 \~"i- ~ "5- !: J .~'5 \ )/t"v i~ \ ·F"" it..,{) ~ ~r:~ 

'"), li1 35 ...., ~ /' .)lt-D (bO .;;~ ;:__...., 

..,. 

1\<C V'"~ 5-<) i b;;l ~?. ~· ~) 

3/ \~ ,,VS" I) lbo )•rc 'i'"i 

3h~ i --;- -,; ~; 

~ ~:; ~-s- ; 

l'=>b 

L 

~ 

":4. 

v a~\ t::7' __ _,. '-..-' 

I Total/ Average 

gjl85 mm 

Type of Trap: 30 i? 

Test End 3i t-1:;( r j 

Date/Time i .:;- : '5 ·5 

Flow Rate 

(cc/min) 

''\-()\') 

t-u::·{-

?(00 

"::.;-()<"-

'1.00 

·.ri) 

?~) ~ 

Dry Gas Meter 

Liters Initial 

~) ,(~~:(~ 

.-;~ ~ 'i/ ~~ 

Dry Gas Meter 

Liters Final 

Chain o~ Custody 

Total Volume 

Pulled 

Relinquished by Tech. :_--'l.._-~.:::..),_· .,_. -_c·_: G""'/'-, __ _._., ~~-~--'i'-'·_/_l_: __ -'}.'-".-·-"'L_· .-_e:t__,: (:;_/_(~_/ ________________ _ Date: f. t - t - • -; 

Received by: ________________________________________________ _ Date: _____________ _ 

Relinquished by: _____________________________________________ _ Date: _____________ _ 

Received for Laboratory by: Date: 

Make-sure all of your sampling conditions prevent moisture condensation in the trap media. Moisture condensation is a major cause of breakthrough and spike 

loss in sorbent traps and should be prevented at all costs. 

For Analysis contact us: 

Ohio Lumex Co., Inc. 9263 Ravenna Road Unit A-3, Twinsburg, OH 44087 USA 

Phone 330-405-0837 Fax 330-405-0847 US Toll Free: 888-876-2611 

Impregnated Activated Carbon- Refer to MSDS 

Deactivated glass and glass wool 
Sorbent Trap 

Chain of Custody 

Plant/Source: ~~~~~~~--~~~------- ~-e.. \ ,.~Y-. <=-. P. 1{ TestLocatl.on·. ( ~ ·· k-..,. f"J· ,--1 -----·~--·-·· __ ·-~'----'~-~,~-~~·~·-------

Boiler ID: .tt ,:) t~ H ----~--~--~-----------------

Trap ID: OL / 5 b DO b 

Trap(JW B <Circle One) 

IZJ Unspiked D Spiked At: 

.. ~/~ 

Certified Accuracy± l 0%, Traceable to NIST 

QA!QC Signature <Trnv M""~l ~~ 

Spike Date: ___ _ Spike Time: ___ _ QA/QC Signature (Spiker) ________ _ 

Estimated Hg in Section 1 : ______ _____,n~g:>-

D High Flow D COIL 

D Static Prefilter D AGS 

I8J.I85 mm 

0240mm 

0300mm 

0450mm 

Sampled By:___;;:C;;.;;..· --....;;~~::....:) 1~: 1_/ ··..~....{ ------- Type ofTrap: ___ ...;;..3.....;0;.......:...;;;5 ____ _ 

Test Start 3- i ") 1 ~ 

(Date/Time :) t,IC- ':'.; 

LeakCheck ~ 

~~/Fail e-;) 5 <~ 

Date Time ~-Temp Sorbent l&oC) ~~mp 

.), . 

,, /r() 

~ tQ ~ d,;.-

~.b "3 5' 

I TotaVA verage 

\~..i'~ 

iiO 

!7 ~· 

\ '1 <i 

7 "7 

;'70 

\ 1"') 

' oq ~~,_<c..; .;r 4 

;;; "5 r.."J 

:;<.··) • _.1 {_.' 

~.? .:.:::: ,.,-.. · .... • ~-· 

#. 

; ) -

,;;. ~-o 

9'S ':) 

Test End ·3- 1• 5' · ;. '3 

(Date/Time) t ~ · i. "SLeak Check e_-, 

Pass/Fail ~~ sFlow Rate 

~fn) 

1-r. -E~(_: .. 

~-t;.o~::..J 

t..j /_)('-

1.-~ t:; -:') 

;-:i c~c·> 

/~~,u 

;.tt:·O 

Dry Gas Meter 

Liters Initial 

(.){. ::.: (. t:J 

~ .. '1 00, 

Dry Gas Meter 

Liters Final 

s, ~;.f!:.!~ 

~o \;::-do 

Total Volume 

Pulled 

Chain of Custody 

Date: "1 - i ~ (J 

Received by:. ____________________________________________________ _ Date: ______________ _ 

Relinquished by:. _______________________________________________ _ Date: ______________ _ 

Received for Laboratory by: Date: 

Make sure all of your sampling conditions prevent moisture condensation in the trap media. Moisture condensation is a major cause of breakthrough and spike 

loss in sorbent traps and should be prevented at all costs. 

For Analysis contact us: 

Ohio Lumex Co., Inc. 9263 Ravenna Roaq Unit A-3, Twinsburg, OH 44087 USA 

Phone 330-405-0837 Fax 330-405-0847 US Toll Free: 888-876-2611 

Impregnated Activated Carbon- Refer to MSDS 

Deactivated glass and glass wool 
Sorbent Trap 

Chain of Custody 

Test Location: .~ ___ :-:: vlJ ,_ .;; \}_jc~ 

Boiler ID: _f""'~~~H--=-·~--b--"".c:::_~l_. _______ _ Trap ID: OL .. 5 b D ~ 7 

[ZJ U nspiked D SpikedAt: 

Certified Accuracy± I 0%, Traceable to NIST 

Spike Date: ___ _ Spike Time: ___ _ 

Estimated Hg in Section 1 : ______ __!n;;:;:g;:>.. 

Trap A Circle One) ~, 

QA/QC Signature <TmpM"'uC~ c:~ 

QAIQC Signature (Spiker) ________ _ 

D High Flow D COIL 

D Static Prefilter D AGS 

181.185 mm 

0240mm 

0300mm 

0450mm 

Sampled By: C.---~U '1 Type ofTrap:. ___ ..;;:;3...;0~6~----

Test Start 6- L'S. -1) 

Date/Time : L 0 ~ t 5 

Leak Chec~ 0 .~ 

ail~0 

Test End '3 - i "£ - 1 3 

Date/Time t 'i/ ', ! c; 

LeakCheck D 

Pass/Fail p::. 'S ~ 

Date Time ~Temp Sorbent Flow Rate Dry Gas Meter Dry Gas Meter Total Volume 

toC) ~/Jemp ~) Liters Initial Liters Final Pulled 

'"--/ oc) 

~- lotS f b·'-o '--;J<1)e:~ f-tCO O,CbG ~ -;;t~2 -/c't f~.~s- II 0 ,:',\~£.:? ·'-fCr? ~ '·:; ~ 2_ ~,u .:c<:;- '•. "' 

3/ L?) 

,, ·- J~' 0 "{']' / 

..- tjVO i ''-~ 5 ':; ,. <..:: i ;;~-:::o !.loJ ~ { ~.., 

" . 

,... ;;J.f t 0'-1 ") /"~ ,, > 1.7 

J ((c::r, i 1 i .. ~i ...._.- "·';o '-LVD ,) • f. 

I '::; tX..~ 

f .. i :; ~· "; ·.:; .- ~. -~- 3 .,:· jf r1J t 7 I ,} ') 2..; P!)V' " j- ' J -1 

. J I ·) . --~ ., c:: .. ·r-o &) ~--o r.>•OO 'V_'J.-;53cJ ,....,-........, C"J'!' i f f -~ ..... b cJ' r. 

.lo I "5 I '5 \- c a-5o &tDO -s- d _Oj_ 7 \ 

'· ) 

I Total/ Average 

Chain of Custody 

Relinquished by Tech.: C j,~ 5i> ~Ldf Date: lt - i - l 3 

Received by:. __________________________ _ Date: _______ _ 

Relinquished by:. ________________________ _ Date: ·---------

Received for Laboratory by: Date: 

Make sure all of your sampling conditions prevent moisture condensation in the trap media. Moisture condensation is a major cause of breakthrough and spike 

loss in sorbent traps and should be prevented at all costs. 

For Analysis contact us: 

Ohio Lumex Co., Inc. 9263 Ravenna Road Unit A-3, Twinsburg, OH 44087 USA 

Phone 330-405-0837 Fax 330-405-0847 US Toll Free: 888-876-2611 

Impregnated Activated Carbon - Refer to MSDS 

Deactivated glass and glass wool 
APPENDIXE 

CALIBRATION DATA 
Dry Gas Meter Box Calibration 

Meter No. 2010 

Baro meter 29.4 Date 04/0 2/13 

PreT est Y 1.0203 Calibrator csm 

Po Vac Vw Tw Vd Td y 

"H20 "Hg ft3 op ft3 op 

1:::u:::: ::::::::m 

0.5 10.000 

0.000 

61 

60 720.339 

730.16 62.5 

60.5 ~· 1.0 189 

l;:r ::ill::' I , .. ·~ ;::.r:lf: ~· · !l!U!!: :iii; 

'I I ·I I T 

1.50 30.000 61 749.72 63 1.0242 

2.00 40.000 61 759.505 64 1.0218 

Average Y = 1.0188 
Dry Gas Meter Box Calibration 

MeterNo. 2010 

Barometer 29.4 Date 04/02/ 

PreTest Y 1.0203 Calibrator csm 

Po Vac Vw Tw Vd Td y 

fP op ft3 op 

0.000 60 720.339 60.5 

10.000 61 730.16 62.5 : ... : : 

: 

... 61 

1.00 

Average Y = 1.0188 
Barometer 29.4 

PreTest Y 1.0468 

Po Vac 

"H20 "Hg 

0.5 

1.00 

Dry Gas Meter Box Calibration 

Meter No. 2010 

Date 

Calibrator 

Vw Tw Vd Td 

ft3 op ft3 op 

0.000 57 174.528 61.5 

10.000 58 184.295 61.5 

10.000 57.5 9.767 61.5 

10.000 58 184.295 61.5 

20.000 58 194.105 61.5 

10.000 58 9.81 61.5 

::::=::::O:U.LU 2o.ooo 58 194.Ios 61.5 

1.50 30.000 58 203.89 61 

02/20113 

csm 

y 

1.0305 

1.0237 

1.0245 

.. !1N#~~~~1i\~~; 1o.ooo 58 9.785 61.25 

:::::i~:::::::::u:S24-------+--3 __ o .. o__ oo-+ ___ 5_8 __ -r __ 2_o3_.8_9 __ r-__ 6_1 __ -F~~~4 2.00 40.000 58 213.625 60.5 1.0275 

"; ,:,so 1 1---------+--~-:-·:~---+---~-;:---+--;:-f-:~-~~-~ --+-- 60~-·?----r~1"""".o"""'o5.:..;.1~ ''' •F======*=== 10o=.:~=~ci===P==~!===*====2;:::::::~·~==56=:5====9== 6=··;==H+&:+++-+.+.BSI 3.00 60.000 58 233.433 61 1.0117 

Average Y = 1.0205 
Barometer 29.3 

PreTest Y 1.0342 

Po Vac 

Dry Gas Meter Box Calibration 

Meter No. 2010 MST 

Vw Tw 

10.000 74 

Date 

Calibrator 

Vd 

9.818 

10/05112 

csm 

Td y 

86 

Average Y = 1.0302 
Barometer 29.35 

PreTest Y 1.0302 

Dry Gas Meter Box Calibration 

Meter No. 2010 MST 

Date 

Calibrator 

Po Vac Vw Tw Vd Td 

"H20 "Hg :ft3 0f :ft3 op 

04/02/13 

csm 

y 

0.5 1 10.000 63 334.735 71 1.0160 

1.00 2 10.000 63 344.685 71 1.0178 

1.50 3 10.000 63 354.6 72 1.0211 

2.00 4 10.000 62 3ll4 ~?~ 73 1.0217 

Average Y = 1.0205 
CHEROKEE INSTRUMENTS INC 

30B Hg Dual Console 

Meter Box Post Calibration 

Cherokee#: 3620 

Meter# Ml-Dual Hg Date: 03/05/13 Operator: J McK 

Serial#: DB 30B-1110-2017 Barometric Pressure: 29.73 in. Hg Vacuum: 0 in. Hg 

HgSide 1 DRY GAS METER VOLUME CALIBRATION DEVICE VOLUME 

Flow Time Initial Final Total Temperature (°F) Initial Final Total Temperature ("F) 

Qmn) (minutes) (Liters) (Liters) (Liters) Initial Final (Liters) (Liters) (Liters) Initial Final 

0.25 40.0 0.00 10.19 10.19 84 85 17883.00 17893.00 10.00 78 78 

0.50 42.0 0.00 21.72 21.72 82 83 I7859AO 17881.50 22.10 77 78 

0.75 31.0 0.00 23.24 23.24 80 81 I7831.20 17854.70 23.50 78 78 

DRY GAS METER VOLUME CALIBRATION DEVICE VOLUME 

Flow Time Initial Final Total Temperature (°F) Initial Final Total Temperature ("F) 

DR!!!.l (minutes) (Liters) (Liters) (Liters) Initial Final (Liters) (Liters) (Liters) Initial Final 

0.25 40.0 0.00 12.22 11.52 78 82 17731.80 17742.60 10.80 76 78 

0.50 35.0 0.00 18.07 18.07 80 82 17745.70 17762.80 17.10 76 77 

0.75 35.0 0.00 27.17 27.17 82 84 17770.20 17796.30 26.10 77 77 

Meter 1 Deviation Meter2 Deviation 

Calibration Gamma (Y)* =I 1.0092 I 1.002 -0.018 0.951 -0.013 

1.035 O.oi5 0.962 -0.002 

1.023 0.003 0.979 0.015 

I A '""'e Grunma--=-- 1.02,;----- -~--=~~amma = --~~-~ 

308 Console-3620 (Dual) 
APPENDIXF 

CHAIN OF CUSTODY 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304} 755-1077 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

LU 

1- SAMPLE DESCRIPTION 0 0 Vi 

z 0 z c.. (INCLUDE MATRIX) 

~ LU LU ~ co 

z !d: ~ <( LU :::1 0 c::: 1- c::: Q i= u l!:} 

1 1 3/15/2013 Baghouse #5 Run 1 Back-half Rinse H2S04 

2 2 3/15/2013 Baghouse #5 Run 2 Back-half Rinse H2S04 

3 3 3115/2013 Baghouse #5 Run 3 Back-half Rinse H2S04 

4 1 3/19/2013 Baghouse #2 Run 1 Back-half Rinse H2S04 

5 2 3/19/2013 Baghouse #2 Run 2 Back-half Rinse H2S04 

6 3 3/19/2013 Baghouse #2 Run 3 Back-half Rinse H2S04 

7 3/27/2013 Blank De-ionized Water 

8 3/27/2013 Blank O.lN H2S04 

9 

10 

1.1) 

c::: 

LU 

u.. z u 

0<( :I: 

=1:1: 1- <( z 1.0 0 N u ~ 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 3/27/2013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS I 

I 

HCI1 of 1 

BH#5 

BH#5 

BH#5 

BH#2 

BH#2 

BH#2 

DATE: TIME: 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

w 

1- SAMPLE DESCRIPTION ci v; 

z ci 0 z (INCLUDE MATRIX) c.. co ::lE w w z ::lE !;;( ::lE <( w => 0 ex: 1- ex: Cl i= u l!) 

1 1 3/13/2013 Baghouse #5 Run 1 Filter 1012 

2 1 3/13/2013 Baghouse #5 Run 1 Front-halfRinse HN03 

3 1 3/13/2013 Baghouse #5 Run 1 Back-half Rinse HN03 

4 2 3/13/2013 Baghouse #5 Run 2 Filter 1011 

5 2 3/13/2013 Baghouse #5 Run 2 Front-half Rinse HN03 

6 2 3113/2013 Baghouse #5 Run 2 Back-half Rinse HN03 

7 3 3/13/2013 Baghouse #5 Run 3 Filter 1010 

8 3 3/13/2013 Baghouse #5 Run 3 Front-half Rinse HN03 

9 3 3/13/2013 Baghouse #5 Run 3 Back-half Rinse HN03 

10 

~ 

ro 

.. 

Q) 

~ 

V') Q) 

ex: c. w ·.;; Ll- z 

0 <C :::J 

:1:1: 1- ~ z "' 0 N 

u ~ 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 3/27/2013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

Metals 1 of 3 

arsenic, 

cadmium, 

chromium, 

manganese, 

nickle, lead 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

DATE: TIME: 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304} 755-1077 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

w 

1- SAMPLE DESCRIPTION d Vi d 0 2 (INCLUDE MATRIX) 2 c.. co ::!: w w 2 ::!: ~ ::!: <( w ::> 0 0:: 1- 0:: Cl i= u l!) 

1 1 3/13/2013 Baghouse #2 Run 1 Filter 1007 

2 1 3/13/2013 Baghouse #2 Run 1 Front-half Rinse HN03 

3 1 3/13/2013 Baghouse #2 Run 1 Back-half Rinse HN03 

4 2 3/13/2013 Baghouse #2 Run 2 Filter 1006 

5 2 3113/2013 Baghouse #2 Run 2 Front-halfRinse HN03 

6 2 3/13/2013 Baghouse #2 Run 2 Back-half Rinse HN03 

7 3 3/13/2013 Baghouse #2 Run 3 Filter 1005 

8 3 3/13/2013 Baghouse #2 Run 3 Front-half Rinse HN03 

9 3 3113/2013 Baghouse #2 Run 3 Back-half Rinse HN03 

10 

...!!! 

ro 

~ 

Q) 

~ 

1./) Q) 

0:: 0.. w :;; u. 2 :::::s 0<( 

=1:1: 1- ~ 2 0'1 0 N 

u ~ 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 3/27/2013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS I 

I 

Metals 2 of 3 

arsenic, 

cadmium, 

chromium, 

manganese, 

nickle, lead 

BH#2 

BH#2 

BH#2 

BH#2 

BH#2 

BH#2 

BH#2 

BH#2 

BH#2 

DATE: TIME: 
~~· • 

TEST, Inc. 

Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

Chain of Custody 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

w 

1- SAMPLE DESCRIPTION d v; d 0 z z (INCLUDE MATRIX) 0.. C'J ::E w w z ::E ~ ::E <( w => 0 0::: 1- 0::: 0 i= u (,!) 

1 1 3/27/2013 Blank Filter 

2 1 3/27/2013 Blank 5%HN0311 0% H202 

3 1 3/27/2013 Blank O.lN HN03 

4 

5 

6 

7 

8 

9 

10 

..!:!! 

rtl 

~ 

CIJ 

~ 

VI CIJ 

0::: 0.. w ·,p u..Z :::::s 0<( 

#I- ~ z O'l 0 N u ~ 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 3/27/2013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

Metals 3 of 3 

arsenic, 

cadmium, 

chromium, 

manganese, 

nickle, lead 

I 

I 

DATE: TIME: 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.corn 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

EMAIL ADDRESS: PCHIN @TESTI NCORP .COM 

LU 

1- SAMPLE DESCRIPTION c:i c:i Vi 

z 0 z c.. (INCLUDE MATRIX) 

::lE LU LU ::lE a::l z ~ ::lE <( LU => 0 c::: 1- c::: c i= u ~ 

1 1 3115/2013 M23/PCB XAD Trap #7, Baghouse#5 Run 1 

2 1 3115/2013 M23/PCB Filter, Baghouse #5 Run 1 

3 2 3/15/2013 M23/PCB Trap #1, Baghouse#5 Run 2 

4 2 3115/2013 M23/PCB Filter, Baghouse #5 Run 2 

5 3 3115/2013 M23/PCB Trap #6, Baghouse#5 Run 3 

6 3 3/15/2013 M23/PCB Filter, Baghouse #5 Run 3 

7 1 3119/2013 M23/PCB Trap #8, Baghouse#2 Run 1 

8 1 3/19/2013 M23/PCB Filter, Baghouse #2 Run 1 

9 2 3/19/2013 M23/PCB Trap #9, Baghouse#2 Run 2 

10 2 3/19/2013 M23/PCB Filter, Baghouse #2 Run 2 

u 

c.. 

......... Vl 

c: 

rtl 

!..... 

:::l 

1.1-

......... Vl 

c: 

·x 

0 

i5 

00 V') N 

c::: ..::t LU r::c LL Z c:::: 

0<( () =1:1: 1-

z m 0 N 

u ~ 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 312712013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

Dioxins I Furansl 

I PCB 1 of 2 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#2 

BH#2 

BH#2 

BH#2 

DATE: TIME: 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

LU 

1- SAMPLE DESCRIPTION 0 0 Vi 

z 0 z (INCLUDE MATRIX) LU c.. l:C :2: LU z :2: !;:( :2: <( LU :::> 0 0:: 1- 0:: Cl i= u I.!J 

1 3 3119/2013 M23/PCB Trap #3, Baghouse#2 Run 3 

2 3 3119/2013 M23/PCB Filter, Baghouse #2 Run 3 

3 3115/2013 M23/PCB Trap #2, Train Blank 

4 3115/2013 M23/PCB Filter, Blank 

5 M23/PCB Trap #4, Not Used 

6 M23/PCB Trap #5, Not used 

7 

8 

9 

10 

u 

c.. 

........ Vl 

c: 

ro 

I.. 

~ 

u. 

........ Vl 

c: 

·x 

0 

i5 

co V'l N 

0:: o::t LU c:c u.. z 0::: 

0 <C 

=1:1: 1- 6 

z m 0 N 

u ~ 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 312712013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

Dioxins I Furans 

I PCB 2 of 2 

BH#2 

BH#2 

Blank 

Blank 

No analysis 

No analysis 

DATE: TIME: 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304} 755-1077 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

w 

I- SAMPLE DESCRIPTION c:i c:i Vi 

z 0 z Q. (INCLUDE MATRIX) 1:0 ~ w w z ~ ~ ~ <( w ::> 0 c::: I- c::: Cl i= u ID 

1 1 3/15/2013 Baghouse #5 DIFIPCB Run 1 Front-half Rinse 

2 1 3/15/2013 Baghouse #5 DIF /PCB Run 1 Back-half Rinse 

3 2 3/15/2013 Baghouse #5 DIFIPCB Run 2 Front-half Rinse 

4 2 3/15/2013 Baghouse #5 DIFIPCB Run 2 Back-halfRinse 

5 3 3/15/2013 Baghouse #5 DIFIPCB Run 3 Front-halfRinse 

6 3 3115/2013 Baghouse #5 DIF /PCB Run 3 Back-half Rinse 

7 1 3119/2013 Baghouse #2 D/F/PCB Run 1 Front-half Rinse 

8 1 3/19/2013 Baghouse #2 DIFIPCB Run 1 Back-half Rinse 

9 2 3119/2013 Baghouse #2 DIFIPCB Run 2 Front-half Rinse 

10 2 3119/2013 Baghouse #2 DIFIPCB Run 2 Back-half Rinse 

u 

c.. 

....... Vl 

c:: 

ro 

~ 

;:, 

Ll-

....... Vl 

c:: 

·x 

0 

i5 

co Vl N 

c::: """ w co 1.1- z c::: 

0 <( <( 

=1:1: I- u 

z m 0 N u ~ 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 312712013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

Dioxins I Furans 

I PCB 1 of 2 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#2 

BH#2 

BH#2 

BH#2 

DATE: TIME: 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

LU 

I- SAMPLE DESCRIPTION d d v; 

z 0 z c.. (INCLUDE MATRIX) co ~ LU LU z ~ ~ ~ <( LU ::> 0 a: I- a: 0 i= u 1.!) 

1 3 3/19/2013 Baghouse #2 D/F/PCB Run 3 Front-half Rinse 

2 3 3/19/2013 Baghouse #2 D/F/PCB Run 3 Back-half Rinse 

3 3/15/2013 Train Blank D/F/PCB Front and back half Rinse 

4 

5 

6 

7 

8 

9 

10 

:c Ill <( 

a: c.. LU ........ LL Z en 

0<( N 

:1:1: I- qz co 

0 0:: 

u <( 

u 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 312712013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

Dioxins I Furans 

I PCB 2 of 2 

BH#2 

BH#2 

Blank 

! 

DATE: TIME: 

I 

I 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

EMAIL ADDRESS: PC HI N @TESTINCORP .COM 

w 

1- SAMPLE DESCRIPTION d d Vi 

z 0 z c.. (INCLUDE MATRIX) co ~ w w z ~ ~ ~ <( w :::> 0 0::: 1- 0::: Cl i= u ~ 

1 1 3114/2013 PAH XAD Trap #5, Baghouse#5 Run 1 

2 1 3/14/2013 P AH Filter, Baghouse #5 Run 1 

3 2 3/14/2013 P AH XAD Trap #8, Baghouse#5 Run 2 

4 2 3/14/2013 PAH Filter, Baghouse #5 Run 2 

5 3 3/14/2013 PAH XAD Trap #1, Baghouse#5 Run 3 

6 3 3114/2013 PAH Filter, Baghouse #5 Run 3 

7 1 3/18/2013 PAH XAD Trap #7, Baghouse#2 Run 1 

8 1 3/18/2013 PAH Filter, Baghouse #2 Run 1 

9 2 3/18/2013 P AH XAD Trap #6, Baghouse#2 Run 2 

10 2 3/18/2013 PAH Filter, Baghouse #2 Run 2 

:I: (,/') <( 

0::: 0.. w ""- u.. z CTI 

0<( N 

=1:1: 1- o:::t 

z t:C 

0 0::: 

u 6 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 3/27/2013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

----------- ---- - ·-

REQUESTED ANALYSIS COMMENTS 

PAH 1 of 2 

BH#5 ' 

BH#5 

BH#5 

BH#5 

BH#5 

BH#5 

BH#2 

BH#2 

BH#2 

BH#2 

DATE: TIME: 
~~· • 

TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-'1 099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

w 

1- SAMPLE DESCRIPTION 0 0 Vi 

2 0 (INCLUDE MATRIX) 2 0. l:C ~ w w 2 ~ !;;( ~ <( w ::> 0 0::: 1- 0::: c i= u <.!) 

1 3 3/18/2013 PAH XAD Trap #9, Baghouse#2 Run 3 

2 3 3/18/2013 PAH Filter, Baghouse #2 Run 3 

3 3/14/2013 P AH XAD Trap #2, Train Blank 

4 3/14/2013 PAH Filter, Train Blank 

5 PAH XAD Trap #3, Not Used 

6 PAH XAD Trap #4, Not used 

7 

8 

9 

10 

:c 

Vl <( 

0::: 0.. w ....... u.. 2 CT'l 

0<( N 

:tl: 1- o::t 

2 c:l 

0::: 0 

u ('; 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 3/27/2013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

PAH 2 of 2 

BH#2 

BH#2 

Blank 

Blank 

No analysis 

No analysis 

DATE: TIME: 
TEST, Inc .. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

www.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

EMAIL ADDRESS: PCHIN @TESTINCORP .COM 

w 

1- SAMPLE DESCRIPTION 0 0 Vi 

0 z z CL (INCLUDE MATRIX) 

:E w w :E co 

z ~ :E <( w => 0 c:: 1- c:: 0 i= u l? 

1 1 3/14/2013 Baghouse #5 PAH Run 1 Front-halfRinse 

2 1 3/14/2013 Baghouse #5 PAH Run 1 Back-halfRinse 

3 2 3/14/2013 Baghouse #5 PAH Run 2 Front-halfRinse 

4 2 3/14/2013 Baghouse #5 PAH Run 2 Back-halfRinse 

5 3 3114/2013 Baghouse #5 PAH Run 3 Front-halfRinse 

6 3 3/14/2013 Baghouse #5 PAH Run 3 Back-halfRinse 

7 1 3/18/2013 Baghouse #2 PAH Run 1 Front-half Rinse 

8 1 3/18/2013 Baghouse #2 P AH Run 1 Back-half Rinse 

9 2 3/18/2013 Baghouse #2 PAH Run 2 Front-halfRinse 

10 2 3/18/2013 Baghouse #2 P AH Run 2 Back-half Rinse 

:c 1./) <( 

c:: a.. w ........ u.. z en 

0 <i: N 

'O:j" ::1:1: 1-

z r::c 

0 c::: 

u <( 

u 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 3/27/2013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

PAH 1 of 2 

BH#5 I 

BH#5 

BH#5 I 

BH#5 

BH#5 

BH#5 I 

BH#2 

BH#2 

BH#2 

BH#2 

DATE: TIME: 
TEST, Inc. 

Chain of Custody Route 2, Box 33 

Poca, West Virginia 25159 

(304) 755-1077, Fx (304) 755-1099 

vvww.testincorp.com 

PROJECT NUMBER: Tl1550 

COMPANY NAME: Felman Productions 

PROJECT MANAGER: Paul Chinuntdet 

PHONE NUMBER: (304) 755-1077 

EMAIL ADDRESS: PCHIN@TESTINCORP.COM 

w 

1- SAMPLE DESCRIPTION 0 0 Vi 

z 0 z c.. (INCLUDE MATRIX) 

:2: w w :2: co 

z ~ :2: <:!: w :::> 0 0::: 1- 0::: 0 i= u 1.9 

1 3 3/18/2013 Baghouse #2 PAH Run 3 Front-halfRinse 

2 3 3/18/2013 Baghouse #2 PAH Run 3 Back-halfRinse 

3 3/14/2013 Train Blank P AH Front and back half Rinse 

4 

5 

6 

7 

8 

9 

10 

:c Vl <( 

0::: c.. w "'- u.. z (j) 

0 <i: N 

-.::!" :tl: 1-

z co 

0 0::: 

u <( 

u 

1 X 

1 X 

1 X 

RELINQUISHED BY: DATE: TIME: RECEIVED AT LABORATORY BY: 

Paul Chinuntdet 3/27/2013 

RECEIVED BY: DATE: TIME: NAME OF LABORATORY: 

REQUESTED ANALYSIS COMMENTS 

PAH 2 of 2 

BH#2 

BH#2 

Blank 

DATE: TIME: 
---....... _.,,.,_,,~ ~ U~E.-·-

rbent Trap Analysis Report 

9nt Name Keika Ventures, LLC 

act Name Lorri White 

9D J.D. Plant/Source Date Analyzed Scientist 

156035 Felman 4/10/2013 John Perko 

150823 Felman 4/10/2013 John Perko 

156060 Felman 4/10/2013 John Perko 

156021 Felman 4/10/2013 John Perko 

156066 Felman 4/10/2013 John Perko 

156064 Felman 4/10/2013 John Perko 

156014 Felman 4/10/2013 John Perko 

150797 Felman 4/10/2013 John Perko 

156042 Felman 4/10/2013 John Perko 

156034 Felman 4/10/2013 John Perko 

156058 Felman 4/10/2013 John Perko 

156006 Felman 4/10/2013 John Perko 

156057 Felman 4/10/2013 John Perko 

156069 Felman 4/10/2013 John Perko 

150824 Felman 4/10/2013 John Perko 

s than 0.027 ng Is corisiaered "< LDL."Which -Is lesstnalf thelowest 

detection limit. 

:atlon Report Available 

mty ±1o% I 

Massng 

Sect1 

0.86 

21.06 

0.67 

0.65 

0.51 

0.73 

0.65 

21.20 

0.61 

19.31 

17.28 

28.22 

26.06 

22.55 

45.09 

VJIIV 1-UIJJC.I\ \JU. 1 IJI\.1. 

9263 Ravenna Rd., Unit A-3 

Twinsburg, OH 44087 

Phone: (330) 405-0837 

Fax: (330) 405-0847 

www.ohiolumex.com 

Project Number 2001307 

D 

D 

Other 

I UJ II • I"'\ I VUIJU I JJJIV 

Standard 

48 hour rush 

Date 4/11/2013 

Phone 919-933-9569 

Massng Massng Spike BreakSect.2 Sect.3 Level (ng) through% Comme. 

0.74 Fie 

0.54 20 Tn: 

0.54 Tn: 

0.61 #5 Baahouse 

0.52 #5 Baghouse 

0.74 #5 Baghouse 

0.55 #5 Baghouse 

0.74 20 #5 Baghouse 

0.47 #5 Baghouse 

0.72 #2 Baghouse 

0.72 #2 Baghouse 

0.87 #2 Baghouse 

0.72 #2 Baghouse 

0.73 #2 Baghouse 

0.57 20 #2 Baghouse 
APPENDIXG 

PLANT OPERATIONAL DATA 
3/18/2013

FCE#2

Time Opened Time Plugged Tap Number Tap Weight Fines Usage Liquid Metal

8:25 8:55 468

10:25 10:55 469

12:25 12:55 470

2:25 2:55 471

4:25 5:00 472

6:25 7:00 473

8:35 9:00 474

10:30 11:00 475

12:35 1:00 476

2:35 3:00 477

4:35 5:00 478

6:25 7:00 479

Total LBS

Total NT

Note: Production and Raw Material data submitted separately as Confidential Business Information

Raw materials consumption

Redacted

With Fines
3/19/2013

FCE#2

Time Opened Time Plugged Tap Number Tap Weight Fines Usage Liquid Metal

8:30 8:55 480

10:30 11:00 481

12:30 1:00 482

2:30 2:55 483

4:30 5:05 484

6:25 6:45 485

8:25 9:00 486

10:35 11:00 487

12:35 1:10 488

2:35 3:00 489

4:35 5:00 490

6:25 6:45 491

Total LBS

Total NT

Note: Production and Raw Material data submitted separately as Confidential Business Information

Redacted

Raw materials consumption

With Fines
3/20/2013

FCE#2

Time Opened Time Plugged Tap Number Tap Weight Fines Usage Liquid Metal

8:45 9:10 492

10:45 11:25 493

1:05 1:45 494

3:20 4:00 495

5:35 6:00 496

7:30 8:00 497

9:40 10:00 498

11:35 10:05 499

1:40 2:10 500

3:30 4:10 501

5:35 6:05 502

Total LBS

Total NT

Note: Production and Raw Material data submitted separately as Confidential Business Information

Redacted

Raw materials consumption

With Fines
SnDo --------------· 

Name: :JEfF K\OC:>wtj"i ____ _ 

(F) IFlldB, (1/2) Yz Fun? (E) lEmpt; 

Date: ---~e, JJ) 13 __________ _ FUME DUST TRANSlFlERRED TO ll ~ :§ftL 

lfime: -~55 -~.:i!l_ ___________ _ 

Tempering Air Temp: 

illlllet Temperature: 

!Baglhlouse BRower __1~~----J?§H 

Tm~rnsfeJr BRower: PSH ----------

Stack Temperatllllre: Air PJressruure: [DO 

MAGNEHELIC GAUGES On Line Cleaning On Line 

No 1 Hopper Pressure ___!_l,_InHzO - .. 5" InH20 No 7 !Hopper Pressure ___t__b__haH!20 

No 2 Hopper Pressure _j:__b__IoH20 _-_l_hBH20 No 8JH!opper Pressure ~hnlhO 

No 3 Hopper Pressure __:!:__h_HnH20 --=l__lnH20 No 9 Hopper Pressure _il,o _ _InH20 

No 4 Hopper Pressure ___i_b_InH20 ~HnH 0 No 10 Hopper Pressure~lnfhO 

No 5 Hopper Pressure ~lnH 0 - .S' InH20 No 11 Hopper Pressure__i_5_hJIHzO 

No 6 Hopper Pressure __±_f,_InHzO _:_L1uH20 

Screw Rotary Bags 

PSK 

CDeall1ling 

-=-l __ [Jlli.!H! 2 0 

~lll1l.!H!z0 

-=l_ __ l!nHzO 

_:_i_!nfhO 

-=-!_Ill1lH20 

On/Off Conve:yor Lock Chute Missing 

No 1 Hopper ON l/ i J_ 0 

No 2 Hopper OtJ J / ../ 0 

No3 Hopper 01\J ,/ "/ ../ __j_ 

No 4 Hopper OtJ ./ / ./ 0 

No 5 Hopper 0/J / / / 0 

No6Hopper oN / / / 0 

• 

No 7 Hopper ON ./ ./ . ./ 0 

No 8 Hopper ON / ../ / I 

No 9 Hopper OM / ,/ ._/ 0 

No 10 Hopper otJ ./ / ../ D 

No 11 Hopper Of\) ~ / v' 0 

EQUIPMENT PROBLEMS _______________________ _ 

MECHANICAL WORK PERFORMED ________________ _ 

COMMENTS: 
B:~G!H!OlJSE, NUMJBHE!R 4! .. d.-

Sino----·----'-"-·-·-··-- .... 

Name: · J\:.FF. Ru>Gv.Jf!L_. 

Date; _---.;)3~·....1..1 g...__~ _.,;1.1">.-0,._.,.e;3~.----_ 

(F) !FuD~, 0 /2) Yz Funn, (JE) lEmrtty 

FUME DUST TRANSFJERRJED TO ~~ :!)H.r\!.• 

Time: · 10:55 ft.W\. 

Tempering Air Temp: Baghollllse Blower 

Tnnnsffer BRower: 

_1.5 ____ PSH 

IDlliet Temperature: !P'SI ·-----·· 

Stack Temperature: Air Press1llre: _lQ_Q__lP'SH 

MAGNEHELIC GAUGES On Line Cleaning On Line 

No 1 Hopper Pressure _±_]_inH20 -,.5 lnH20 No 7 Hopper Pressure _t_linHzO 

No 2 Hopper Press1llre __±_]_lnH20 _:_l_lnH20 No 8 Hoppew Pwessure ~lnHzO 

No 3 Hopper Pressure _±_}_InH20 -=-l_InllhO No 9 Hoppew Pressure + 7 lnH20 

No 4 Hopper Pressure+ b 5 InH20 _:_!__InH20 No 10 Hoppew PressMre__:t1_l!nHzO 

No 5 Hopper Pressure.\.~ InH20 - .. S InH20 No tl Hopper Pressure A lnH20 

No 6 Hopper Pressure _!_]_lnH20 -=l_lnH20 

Screw Rotary Bags 

CBeannng 

=-l_KnH20 

.-f HnH[zO 

::.J_huHzO 

-=l_RnlH.20 

_:.:_/_hnHzO 

On/Off ConveJ::or Lock Chute Missing 

No 1 Hopper ()tJ ~I ./ -7- 0 

No 2 Hopper OrJ .J / 0 

No3 Hopper ON ./ ./ J I 

No 4 Hopper. OA.l ./ .L / 0 

No 5 Hopper otJ ./ J v 0 

No6Hopper otJ ~L / _/ 0 

No 7 Hopper o~l J / v' 0 

No SHopper ()tJ / / .; I 

No 9Hopper OtJ ~I ~I / Q 

No 10 Hopper ON ./ ~ / 0 

No 11 Hopper o,J / ../ v 0 

EQUIPMENT PROBLEMS._~---------------------

----------------------------------···---

MECHANICAL WORK PERFORMED 

COMMENTS: 
Snno ·----·-·-------

Name: -~~E'"'-f~f___.R~\D...,b..._uJ~f)~i __ 

Date: 3 _-I~- J,.O 13 

(F) FaA~~. (l/2) y; !FUABI, (E) Emplt) 

FlUME DUST TRANSFERRED TO Fl J. :<ml •: '· 

Time: 11:55 A ,(Vl. 

Tempering Air Temp: 

Inlet Temperature: 

___ oF 

ow 

lBagllno!U!se Blower 

T!rams1fer BDower: 

_L_$" __ PSH 

PSH --- -----·-

Stack Temperature: ow Anlr P~ressttme: j.Qn__lP'Si 

MAGNEHELIC GAUGES On Line Cleaning On Line 

No 1 Hopper Pressure __±__fo__InH20 ~InH 0 No 7 Hopper Pressure i..k_..,S_InHzO 

No 2 Hopper Pressure ~InH 0 -=-l_InH20 No 8 Hopper Pressmre ~InHzO 

No.3 Hopper Pressure +b S InH20 _:_l_hoH20 No 9 Hopper Pressure ~inHzO 

No 4 Hopper Pressure __±_k_InH20 -=-l_InHzO No JO Hopper Pressure~inHzO 

No 5 Hopper Pressure+' .S InH20 ~InH 0 No tt Hoppe1r Pressure ;- S InH20 

No 6 Hopper Pressure -=tk_InHzO _::_l_tnHzO 

Screw Rotary Bags 

Cleamil:llg 

_::__l__ BnH20 

~lnHizO 

_:l_ __ linH20 

_::j_n nflhO 

_:::_1__ hniH!zO 

On/Off Convexor Lock 

~ Missing 

No 1 Hopper otJ 

~ .I 0 

No2 Hopper ON ./ 0 

No3 Hopper ON / v / l 

No 4Hopper otJ ./ ./ ./ () 

No SHopper orJ / / ,/ 0 

No 6 Hopper f)j\) ,/ ./ / 0 

No 7 Hopper otJ ./ ,/ ,/ () .. No SHopper ON L ./ .. L I 

No 9 Hopper ({)N t/ vi 1/ 0 

No 10 Hopper Q{\) ./ ~ / 0 

No 11 Hopper orJ ,L_· J ../ 0 

EQUIPMENT PROBLEMS _______________________ _ 

MECHANICAL WORK PERFORMED 

COMMENTS: 

-- .. ...; 
BAG!H(HJSF' NUMBER: -tl d.-. 

Name: 1-t.t=F-__ RJ-DG\.J~i Date: __ 3_l~_:_¢Q_ L3 

Time:~ 55 P .. ~«<--=.......-___ _ 

Tempering Air Temp: 

Inlet Temperature: 

Stack Temperahure: 

Snno -------·- ----· . ---

(JF} Fo.nnn. (1/2) Yz !FudD, (IE) Emp1ty 

FUME DUST TRANSFEJRJRJED TO __ 1:1 ~ :'W1_ ·':· 

JBagiJ:nOII.USe JBDower 

Tmnsfer BDower: 

Air Press\Ulre: 

_L_S ___ Pm 

IP'SH ··---------

_\_Ql)__IP'SB 

MAGNEHELIC GAUGES On Line Cleaning On Line Cleaning 

-=.._{ _B'1111H20 

=-1_ hul!-i!J,O 

-=j__B1111H20 

=-l_ I nll-izO 

~j__ __ ID1lH20 

No 1 Hopper Pressll.llre -:!:..k.5:._In.H20 - • .5" InH20 No 7 Hopper Pressllllre tfo_! .. :S.JnH20 

No 2 Hopper Pressure~ b.S lnH20 =-J_InH20 No 8 Hopper Pressure -1-b ,5InH20 

No 3 Hopper Pressure ~InH 0 _:_l_lnH20 No 9 Hopper Pressure ~inHzO 

No 4 Hopper Pressure _.::!:__k_InH20 _::_LinH20 No to Hopper Pressure-+.-G:,,S inH20 

No 5 Hopper Pressure+~ ,S InH20 ..,.. • 0 InH20 No 11 Hopper Pressure_!___§_bnHzO 

No 6 Hopper Pressure -1-- b. S In.HzO -=-L_ InH20 

No 1 Hopper 

No 2 Hopper 

No3 Hopper 

No 4 Hopper 

No 5 Hopper 

No 6Hopper 

No 7 Hopper 

No SHopper 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

On/Off 

o#J 

ON 

ON 

ON 

otJ 

()t.J 

ON 

OtJ 

OrJ 

ON 

ON 

Screw 

Conveyor 

j 

I 

./ 

/ 

/ 

Rotary 

Lock 

/ 

/ 

/ 

./ 

/ 

/ 

/ 

./ 

/ 

./ 

/ 

~· ... 

/ ... 

Bags 

Missing 

() 

0 

I 

0 

0 

0 

C) 

I 

0 

() 

Q 

EQUIPMENT PROBLEMS. _________________________ .. _______ _ 

MECHANICAL WORK PERFORMED _____________________ _ 

COMMENTS: 
Sillo ·-~--- -~·-·· .... ···--· 

(JF) lFIIllfii, ( J!/2) Yi Fullll, (IE) ~t<:mpt; 

FUME DUST TRANSfi'!ERRED TO 

Tempering Air Temp: 

lnBet Temperature: 

___ "F 

"F 

Baghm.11se BRower 

Translfer BRower: 

_l_l_S__PSH 

lP'SH --- --------

Stack 'femperatmre: "F --- Air Pressure: j_Ql.)_ lP'SU 

MAGNEHELIC GAUGES On Line Cleallling Olll Lnne 

No l Hopper Pressure .i._k_InH20 :_tz..S:.JnHzO No 7 Hopper Pressuure _±j,_InfhO 

No 2 Hopper Pressure _±.]_1nH20 -=J_InH20 No 8 Hoppell" Pressull"e ~lnHzO 

No 3 Hopper Pressure _±_llnH20 ...:::_LinH20 No 9 Hopper Pnessul!lf'e _-t_l_InHzO 

No 4 Hopper Pressure -+ {a inH20 -=:l_!nH20 No 10 Hoppell" Pressure"!-~ .5' lnH20 

No 5 Hopper Pressure +! InH20 =+-InH20 No 11 Hopper IPressure~lnHzO 

No 6 Hopper Pressure _k_d_InH20 _::l_lnHzO 

Screw Rotary Bags 

Cleaning 

.. ::J ____ ll.lli1H20 

--=-'-KnlHI 20 

-=--LHnH20 

.=_!_lnH20 

-=i __ Hlrn!HbO 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper ON J / I 0 

No 2 Hopper ON J ./ I () 

No3 Hopper ON / ,/ J \ 

No 4 Hopper orJ .J / / 0 

No 5 Hopper Ql\) ·L ..1 J 0 

No 6 Hopper o&0 ,_/... .I / 0 

No 7 Hopper QrJ ~/ ./ ,/ D 

No SHopper orJ ~t.. / J I 

No 9 Hopper t)rJ ./ .. / / (.) 

.) .. No 10 Hopper 01\J ,/ / D 

No 11 Hopper I() 1\) ./ / I () 

EQUIPMENT PROBLEMS. ______________________ _ 

MECHANICAL WORK PERFORMED __________________________ _ 

COMMENTS: 
Snno --~--------------- (F) F~Hi, (1/2) ~ FudH, (E) !Emptr·; 

FUME InJST TRANSFJE.RRED TO __ #_J,_ SH ... 

/ 

Tempering Air Temp: !Baglhtol!llse BB~we_r 

Transfer. BRower: 

_L,.S _____ )P'S n 

Inlet Temperature: 

Stack Temperatmre: Air Piressume: 

MAGNEHELIC GAUGES On Line Cleaning . On Line ...... . 

No I Hopper Pressure~I.nH 0 - .~ InHiO No 7 Hopper Pressure _±1_InH!20 

No 2 Hopper Pressure· _±_]_inH20 --=l_InH20 No 8 Hoppen:: ·Pressure +C..S InHzO 

No 3 Hopper Pressure~_lnJ-1 0 -=-l__InHzO No 9 Hoppe~ Pres~re .!.b_,S)nlHzO 

No 4 Hopper Pressure ~lnH 0 -=-l_InH20 No !0 Hopper Pressure...:tJ:u2inH20 

No 5 Hopper Pr.essur~ ~inH 0 - ~S lnH20 N~ H .Hopp~r PtessUJure~hnlhO 

No 6 .Hopper Pressure + b 5 lnH20 _:::_LjlnHzO 

Screw Rotary. Bags 

lP'SH 

CDeaning 

-I ln.H. 20 

_-_l_lnll·llzO 

-=:__l ____ huthO 

-=L_nnlHzO 

-=-1-InlH~.o 

On/Off Conve::ror Lock Chute Missing 

No 1 Hopper otJ j ~{_ / 0 

No2 Hopper ON / .I / 0 

No 3 Hopper OrJ / / ,/ 

No 4 Hopper f OtJ ,/ / I 0 v . No 5 Hopper · o~J ,/ J / () 

J • 

No 6 Hopper ON / / 0 

No 7 Hopper ON L- ,/ / D 

No8Hopper Ot~> / -1- -+ I 

No 9 Hopper otJ ~ 0 

No 10 Hopper ot-> -/;_ / /J 0 

No 11 Hopper OJ\j I / / () ... 

EQUIPMENT PROBLEMS ______________________ _ 

MECHANICAL WORK PERFORMED ·--------......,------------------. 

COMMENTS: ----------------------------------------
N21me: ---~E...rr__R~~~\~~----­

DSJte; _'J :J-1{~--Q.-------------- __ 

Tum.e· _ _ __ _3_:~-~Q __ J'_:JY) ~------------

Tem!fH~lfillllg Air Temp: 

II!lliet Tempemtuwe: 

!Bmg!hloll!lse imoweff 

Tmn§!fe~r imowea: 

_.';,;:: 

Sta<ek Tempewatmre: 

___ "F 

"JF Anw PwessiUlrrre: \00 PSH 

MAGNEHEUC GAUGES On Une Cleaning On Liil!lle 

No » Hoppew PresslU!rne j:___:]_htH20 - .. .$" hnH20 No 7 Hojpper JP'wessilllrre 1:-- 7 iJrnlHhO 

No 2 Hoppew Pressaue __:!:__linfll20 ---=l_hnlH{zO No 8 Hoppelf' lP'wesslllline _±_l_h11lHhO 

No 3 Hoppelf' Pressure _:t__2InH20 -=--l_hnl-l[zO N<O 9 Hopper Pressame _±__]_hulH!20 

No 4 Hopper Pressuwe ____±_la__InH20 =--l_InH20 No to Hopper PrressiU!Jre_±]_I!DlHzO 

No 5 Hopper Pressure -+ l InEbO -.!:; InllhO No 11 Hopper Pressu.nre _tk_ llllllHI20 

No 6 Hopjper Pressure -\-·l InHzO -=l_lllllH[zO 

Scwew Rotary Bags 

CHealllling 

---=J ___ lllffi ~n ~ <O 

~- H mill-ll 2f)i 

_:_LY li111Hh0 

-/ HnH20 

--=-J-hlllf-lH J 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper Ob.J I I T 0 

No 2 Hopper otJ J J / 0 

No 3 Hoppew 6~ J J ./ I 

No 4 Hopper otJ J J ', 0 

No 5 Hopper O!V vi 0 

No 6 Hoppew otJ ./ ./ / 0 

No 7Hoppew otJ J ,_/ ./ 0 

No 8 Hopper O/'J ../ ._/ ,/ I 

No 9 Hopper orJ .,/ ,/ / 0 

No 10 Hopper otJ J ,/_ ,/ 0 

No 11 Hopper oJ J / I 0 

EQUIPMENT PROBLEMS. _____________________________ ~--

MECHANICAL WORK PERFORMED 

COMMENTS: 
~l-~ "t, .1':.'1. R .· R 'k 'Ill J;l J::L.: "", , M ""'-· !.t .: .~ I' J.' Ill II! •·. ~ !/ .~ I;{ !/ R" 

BA(;HOlJSJE t\lt:MBlf~R ·--· ·----··- i:! ~ -· . 

SnDo --------·-----··· 

(F) F\Ulni, (J/2) ~ F\UIDR, (IE) JEmpt} 

Name:_ :YEEF R 1\J GWA'i 

Dtat~e:. 3 -• 0 -·--~---c:/:!!---- • ' 0 \.3 ---· ·-----·- FUME DUST TRANSFJEJRRED TO--~-~_ SHL(;, 

Time: ______ lt~_.:S:Q. ... t~ VV!~-- _____ _ 

Tempering Air Temp: 

!niet Temperat111re: 

Stack Temperature: 

OF ---

___ oF 

OF ---

Baglnouse lBDower 

Transfer Blower: 

Anr PressMil"e: 

d . '() JP'SR 

PSH ----

-10 0 PSH 

MAGNEHEUC GAUGES On LiMe Cleaning On Lnne CYeaning 

. No 1 Hopper Pressure + / in:U20 ._. 5 InH20 No 7 Hopper Pressmre __:!_LinHzO -=~_{_lnH 0 

No 2 Hopper Pressure _:tllnH20 --=-l_InH20 No 8 Hopper Pressure ~inHzO 

No 3 Hopper Pressure _t]JnH20 -=i-huH20 No 9 Hoppel!" Pressure _8hnHzO 

No 4 Hopper Pressure ~inH 0 _::_LinH20 No 10 Hopper Pressunre_j:_]_InHzO 

No 5 Hopper Pressure + flnH20 ..:::..__,_£inH20 No II Hopper Pressure ____±_hlnHzO 

--=--L._ HnlHI2 0 

-=-l_huH20 

~inl-hO 

_::l_InlhO 

No 6 Hopper Pressure + linHzO -=--linHzO 

'-'~\ .... ~. 

Screw Rotary Bags .. 

On/Off Conveyor 

No 1 Hopper CN J 

No 2 Hopper () r-J J 

No3 Hopper _o.bl_ ,/ 

No 4 Hopper ON 

No 5 Hopper otJ -+ 

No 6 Hopper ON ~ 

No 7 Hopper ON / 

No 8 Hopper (jt\} J 

Lock Chute Missing' 

J 7 0 

J / 0 

J --1- __ I_ 

J 0 

~- / () 

/ /-- 0 

J / 0 

J / I 

No 9 Hopper OIJ / ,/ / 0 

No 10 Hopper 'DN v' 

No II Hopper orJ ./ 

J ~ () 

7 / 0 

J 81'1(, ·• 

EQUIPMENT PROBLEMS ______________________ _ 

MECHANICAL WORK PERFORMED ---------------------------------------

COMMENTS: 
BAGHOUSE NUMBER: ---~J__-~-

Silo _____ _ 

(F) Full, (112) Yz FuBB, (E) Empty 

N arne: _...J~E:.L.!H:__g_~' o::...::c.:_::.w..c.:fl'-'-'1_.__ __ 

Date: -~~!--..!.l...:::~~--'~~O-=L3~--- FUME DUST TRANSFERRED TO-·-~ SILO 

Time: _5~: Y..L:O::::__:'P.__._,f'o....__ ___ _ 

Tempering Air Temp: lBaghouse Blower I.S 

Inlet Temperature: Transfer Blower: 

Stack Temperature: Air Pressure: 1oa 

MAGNEHELIC GAUGES On Line Cleaning On Line 

No 1 Hopper Pressure i]_InH20 -.,S' InH20 No 7 Hopper Pressure _ilinH20 

No 2 Hopper Pressure _:t]_InH20 -=l_InH20 No 8 Hopper Pressure ...±k-InH20 

No 3 Hopper Pressure ~lnH 0 _-_I_InH20 No 9 Hopper Pressure _±.::ZJnH20 

No 4 Hopper Pressure ~lnH 0 -=-l_InH20 No 10 Hopper Pressure__::!:_l.InH20 

No 5 Hopper Pressure _±_}_ lnH20 ~ .,5 lnH20 No 11 Hopper Pressure + 5 InH20 

No 6 Hopper Pressure __±]_ InH20 -=1_ InH20 

Screw Rotary Bags 

PSI 

PSI 

PSI 

Cleaning 

-=-l_InH20 

--=-i_InH20 

.::l_InH20 

-=l_1nH20 

-=l_InH20 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper DN J 7 --;' CJ 

No 2 Hopper ON J J / Q 

No 3 Hopper 0/\J J ~/ ./ I 

No4 Hopper ON l/ / / 0 

No 5 Hopper ()/J ~/ / / 0 

No 6 Hopper ()I\) / / ,,./ 0 

No 7 Hopper 01\J / ,/ / 0 

No 8 Hopper nN / ,/ 

.. L 

No 9 Hopper ON J ,/ / a 

No 10 Hopper OtV / / ,/ (') 

No 11 Hopper ar.J J / / 0 

EQUWMENTPROBLEMS _________________________________________ _ .~ .. 

MECHANICAL WORK PERFORMED ___________________________________ -'----

COMMENTS: 
; 

ii-I ftMf>~ t\ ".1!, •. : . :_, PRJ. f~tJ 

l .. ,-

.J ~J rl,j\'). 3~o 

Iii ;U H,•ll 

310 

330 

340 

R ttl. 350 

345 

14 '(f)· 3qo 

. :. ('! f VV\. 3?>0 

' c_ :) tN\ -·.... .. l . V; I. 

a.. f~\. fM) A'fi'lf5 t:J 

3,~o 

3J.O 

3 ;;1.0 

3110 

350 

3'1 0 

340 

33,o 

330 

330 

330 

I O~rlf!Er<. 

ss 

57 

bO 

bD 

too 

bO 

bO 

{pQ 

I .· ·, t.? ij 

,, :~ , . 
,.. - iiY\11:. 

I: 10 f.VY).i_l _~ ____ j!:/O __________ ..... 'l 

_!..(0 f.Vll:, 

,. ~ '' ·--· ~----- --· 0' -- -- N~ .... ,-.,-•• ~,o.,,,,_,, -

' l .55 (ttl;; 3YD 'f't . ---·- .. ------~---··-··- -~---------~ --~---------~-~ ,. -. 

... .;. 

3'-IO 

~l{D ... ---···--- .. -. ·- - -

,. 

f. f\l ' j - __ 3~_0 ___________ ,. ____ .. . . J ,_ ... -- -- 1'1 i l 

. ' 

~ . ! 0 f. VV\• ' 

'--~ l 

' 

~ ... ---- ·- -------- -· .... ·---------··----------------

3.l'O 

330 

! '. -:-· ---~--- -------------- ·--·-···--· 

'. I I 

·- ------------------- ·- .-.--. _,..__-

~\ _i }' 

33o 

330 

_33S 

33() 

(.O 

bO 

ft,_O 

bi:J 
3 -113 - J-01 3 

;: : ..1:j fV"! 3\o 3\0 60 

' 

·j c ·, i ~) ,J f.v¥1. ~JQ_ 3JD k,o 

-' ~---- -- ---- --- -·-- .. , ___ . ---

. ,_ :o f.VVl, 3;,g ~J-'0 ~0 

3;;1.0 too 

00 

··- ss ~m~.: ~30 3J.D bD .. , 

~· 

tl 

l~ ID p ' ~ .Y'). _3_J__Q ___ ,, 3JD roo 

'j 

.:.---t ··-----------------------·-- ---------------- :I 
f ''•' 

" - I ._,, , ! I :.7 -" .) --·-·· 

.. 

< ..... ,., 

...... _, . ·--" 

350 

330 

33o 

330 

]YO 

.. 

·' 

330 

33D 

330 

/ ; l 

(} -~ 

( :,J Q: 

Si 

$<a-. 

5~ 

ss 

59 

~ 'iD 5 ~ 

- . 

ss 

.... I ·~ ,so f.w\. . ___ }t-to ·----------~. 330 s~_ -~--

-__ l . o :5 f. \"f\~. 3tP 33_9'" ,::; 8 ___ so 

··-----~ ·. -~--~~<-~~===~3~~0,. ___ ,.__ ---~--~3:..:,.:!./ D:::,_· -"""""""'"""""""'----.,;Zs_~_cg;:..c ........_---~~~• --...=:-

·-· _lj'.QQf~ , _________ .}.~(? --------- ~tl_Q ____ _ 

-- !..\ ·.(5 f (11 ..• . .... ,_31() 

j. ~t../-0 

3JQ. 

-3o J .... - -- -- ., -

7t.jO . ;1 ----

2g_· ---- ·------~-- --

5(') . ...D............. . 

._._;;p __ 

_;i_Q58 ----·--- ------- ___ SQ 

.... -------·------------------ ______ .3...2.g _________________ , _______________________ ...... S_R __________ . ____________ so _ 3JQ _________________ ~-------- ____ __ _ ss~ ________ _ ~tli ·······-------~~ 

58 ~;,, 
/ 

(1) ·~ -I ·-..J 

-- t:l: :!pi.t 1-t,v 

) 58 3lfO 

. ···~~-·--· ·-~-·· .... ··- ..... ---······· ····~--~-· --.-----

------·····---·----· ---------- .... -···"· --·-·-····--·-··--·--------·--·· --------·-- I 

·-----------·-·----------.... .. --· ... -. ·- -·--·· ----·- ------------------·-··- .. -----·---- ----···- --- --·-··--·· .. -· -········---. ·I 

. - -- -·- - --· -· -· -·------ ··-· ... . -·--·····-· - .. ·- . . - - --- - - ~~~~ I 

--------------- ---------------· -· --------------------------·-· . .II 

·---~-. ------· ........ --·····---- -·--- -----.. -- ·-------- -·--· --······--·-··•>-····-~~~--~---~-~~~--~~-~-:~ --~~~·:-~-~--~--:.~.~~~~~~~~~-· :~-----. ··---~~·~=- ···--·---~---~~~ ........................... _II -- ......... ---- ... -----·- .. -·- ............ --- ·-------·--------·-··- ----............ ------·-· ------ ·I 

----.. --------- ... ---- -- ....... -... -- -. -----------·- .. ---··. ----........ -- --- ...... --- -----.. ·-- -------·-- -- --···---·----- ----------- I 

.. 

~ t ... 

.! I! I ------~--------- --r+~--:-~-~-··----............. -~~·"·~ .. ··~-~---~--· .... ~ . .-.-.- ~-~-. ~·,.·----·~-~·-- ----·~- ...... ~·-·--- ~.:------... ~--~-~-----·---~:---~.:..·---· ·-~----, ---~ ---~-~; . ___ , ____ -·- ·-· ---~------

------------- ------·------ ·-· ---··----------····--···-·- ------.. - ,' I .. 

1-.L. 

'' 

"~ .... ~-- .. - I • 

i' ll 

. ......... ---·-··--····-·-·· --- ------ -·-··-- --- .......... -. ----------··· .. ~~~~~~~-~-· ..... ------~~~~~~-- ---~~~--- -~ ~-~~-~~--~- ---~--·~--~~= ll 
hniet Tenlf"l))<elT'>ntilllJr<e: 

Stack 1\empen~h''ir"'' 

~ 

"If 

)JF 

...... ~ i t: 

tB1llglhH)lil§i:: liUO>'N<efi' 

T!r2l[a§if,e;r iafi!())'~h't=e: 

MAGNEHEUC GAUGES Oilll Lilllle Clemlllliilllg On Liiille 

No ll JH!oppew Press\Lme ~IIllilHl 0 __ :": hn.HhO No 7 Hoppew Ptr<eSSil!llr'<e -t -:_rrnH,O 

No 2 Hoppeir lP'JreS:<Jillllfe ______:_]_ hnlf:ll20 __:':::__j___ iilllll--llzO No 8 Hoppe:r Pressu1ne t- 7 hilHzO 

No 3 lH!oppen PnessiL~Ir<e + l !nlhO ~ , hdi! 20 No 9 lH!oppe:r Pressrunre _i____]_hnllzO 

No 4 Hopper PoeSSiJJir<e ~InH 0 - 1 i!!lllHI20 No 10 Hoppu Pressrunre +- 7lirnil--li_z0 

No 5 Hopper- lP'IfeSSillllre ~InlHl 0 ~. S" lnH20 No I~ Hopper lP'Jress\lllre + 5IIIllHzO 

No 6 Hopper lP'wessQJlre -t { !llllH20 _::_L_IlllllH!20 

Rotary Bags 

;r: f 

. ~ fi___. 1 ) 

Cieani!tllg 

~' _IIlllH20 

illll!H20 

~hnH 0 

__ l!lllllH!zO 

_ __,_lllllH20 

Oll1l/Off 

Screw 

Conveyor Lock Chute Missing 

No 1 Hopper orv 

No 2 Hopper 061 

No 3 Hoppew CtJ 

No 4 Hopper CJ/J 

No 5 Hopper o/J 

No 6 Hopper tr'H.J 

No 7 Hopper (')~) 

No 8 Hopper ()1\J 

No 9 Hopper 0 !\j 

No 10 Hopper 01\) 

No 1] Hopper O!J 

f 

I '\..,/ 

I ./ 

-/ 

/ 

j 

/ 

,./ 

/ 

./ 

I 

/ 

,/ 

/ 

,_/ 

./ 

J 

/ 

/ 

_/ 

J Q 

_L a 

/ l 

/ 0 

/ 0 

/ . ./ Q 

/ 0 

/ I 

,_./ 0 

/ 0 

j 0 

~8~(~ 

EQUIPMENT PROBLEMS. _________________________ _ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
;. __ g_::; '•'-

h'hlei f'ctmp:e;r:rut;u:~'~ 

:S taH: k if,£ m pe ra lt!l!l <":£ 

::_:• 

__-·-, ,-

MAGNJEHJEUC GAUGES Olll Ulllite Ueallllirng Ol!ll L,!irM: Cfieami!P'$ rl 

No X lHloi!JipH P:ressl!lltre + ~ hnlHl20 _:.~)_b,H 0 No 7 HoppeR' P:re§SiJ.Dtre _±_lV:ndHI20 __ -=::} ___ 1tll1lH20 

No 2 Hopperr lPr~ess!l!ltre _-\- r< hnHzO 11lRlHi 20 No § Hopper Pre§S\Uiine +- X ~illl-llzO Rnlf-hO 

No 3 JH!oppeir lP'Ifessture -1 Q, h11JH! 20 Hl!1lJH! 20 No 9 Hopper lP'If<::SStuilre -~-~hnlHI 0 Ul!1lH:O 

No 4 Hopper~ Pres§IU!ifte -~ 7 Kll1llHh0 -=-l_h'llH20 No dJ Hoppn Pressll!llne + 7Sl!HilH20 ~lillH 0 

No 5 Hopper lP'rressrunre _2 _ _3_I:rnlHiz0 - p =: inH20 No n Hopperr JP'ress\Uire + r,~Kil1lH () hnlf-l!zO 

No 6 Hop!fl!<?tr PH""essllilwe -': l.S llll1lflh0 Ull1lll-llz0 

Screw Rot21ry Bags 

O~rn/Off CoiDrveyor jl,A:»ck Chute Missing 

No 1 Hopper C/<J ,/· __J_ j 0 

No 2 Hoppes- OrJ ·,/ -/i J :; 

No 3 Hoppelf orJ j / ./ 

No 4 Hopper OrJ ._.,/ ./ _L_ "" v 

No 5 Hopper C1rJ I i ./ C: ~-·-

No 6 Hopper ON / -~L_ ,/ 

No 7 Hopper Q/'J _ _L__ ___/ _ r· 

·• . ....-· 

No 8 Hopper Or,) / _L__ _.L_ 

No 9 Hopper f) tJ / /' / f'\ 

~· ---

No H) Hopper OtJ .. / / / 0 ---

No lll Hopper oJ / / 

./ / 0_ 

~13~~ 

EQUWMENTPROBLEMS _______________________________ _ 

MECHANICAL WORK PERFORMED ______________________ _ 

COMMENTS: 
_ j::__;;:_ __ Q ,JQC:v.Jt-1 t 

-3. : ~~ .... ,j., r..:~. ; ::,_ 

' . : ·~ 

; ' ~.-- ~. 

____ J... 

FM 

l £m.p><eriflllg A Jr. Temp 

haid Tempewah.1re; 

Stack Tempen!ltmre: 

Ragllunnse Blow!':• 

Twali1ls1fer Blm'VIt';r· 

Aiw Pressru11re: :_-:_)_Q ____ PS~ 

MAGNEHEUC GAUGES Oi!! Line Cleaning On Line 

No 1 Hopper Pressure ~[nH 0 - ,.5" InH20 No 7 Hopper Pressll!lre _±_2_inH20 

No 2 Hopper Pressure ~lnHzO -=-i _lnHzO No SHopper Pressure ~~h:aHzO 

No 3 Hopper Pressure ~lnl-llzO _::_l_hulhO No 9 Hopper Pressure _i_h_imlllhO 

No 4 Hopper Pressure 26_InlHzO _::_l_InH20 No 10 Hopper Press1111re.:Ut'-~-~nH 0 

No 5 Hopper Pressure _±l hnHzO - .. 5 lnHzO No n Hopper Pressure _!-_5_1nl-!h0 

No 6 Hopper Pressure _:t_h_InHzO _-:J_hllHzO 

Screw Rotary Rags 

Cleaning 

-=_L_ __ InH20 

_ _::-_L __ InH20 

::.L_hnHzO 

_-j_ __ InHzO 

-1 hnl-hO 

On/Off Conve:yor Lock Chute Missing 

No 1 Hopper Of..,) ./ J J 0 

No 2 Hopper OIV / / / 0 

No 3 Hopper 0/V ~/ / v 

No 4 Hopper 0/\1 ,/ ,/ ~ 0 

No SHopper OtJ ./ J ./ 0 

No 6 Hopper ON ,/ _L_ / 0 

No 7 Hopper OtJ / ,/ / 0 

" 

No 8 Hopper _ill)_ ./ ,/ L I 

No 9Hopper orJ ./ _-L_ ./ () 

No 10 Hopper o,.J \/ ../ ./ 0 

No 11 Hopper ON v / ~ 0 

~&x,s 

EQUIPMENT PROBLEMS 

MECHANICAL WORK PERFORMED ___ ~----------------

COMMENTS: 
' J '! 

MAGNEHEUC GAUGES Ollii Lilllle ClemiDlil!ll2 On Ulllie 

No 1 Hopper PressiDJre _!~l_h11lH{zO ~ .5 ~hllH 0 No 7 lH!O!tiJP<e!r Pressmne __!_]_hn!Hl20 

No 2 :Hoppew Pwesswre _t_2_hlll-!i 20 .= __ : h:LlHl 20 No 8 Hopper Pwessmre~5 h:nllbO 

No 3 Hopper lPn:ssunre __ ±]_hn!H20 -=l_fflllllH20 No 9 !Hopper lP'n:ssiiJlre _ + ]_lillllH20 

No 4 Hopper lP'ressmre r b .5IirulHlz0 -=1_ hlllf-hO No no Hoppe;r lP'rressllilre _"!_]__ linlllHhO 

No• SHopper lPressuure i- l_lllllH20 - .,5InlHlzO l'<lo n Hopper lPressure _ _±S_IililHhO 

No 6 lH!op!=;eJr Presslll!Jre ~ l h1H20 - \ illlllHzO 

Screw Rota;y Bags 

, .• .,;._ 

~~~eailllnrmg 

-~j_llllllH 0 

_=l__htlH! 20 

:" __ L IllllllhO 

__ --:_L_ !illlHlzO 

-=L ___ N illllH!,o 

Ollll/Oflf CoJIJiveyor Lock Chute Missing 

No l! Hopper otJ \1 J ,/ 0 

No 2 Hoppew orJ / / .,_/" 0 

No 3 Hopper oJ / / ./ 

No 4 Hopper otJ ./ / ./ 0 ---

No 5 Hoppew Dt.J ./ _L_ / 0 

No 6 Hopper f)!J J' ./ ./ 0 

N<D> 7 Hopper OtJ / / / C) 

No 8 Hoppeir ()tJ ./ / ./ --

I 

No 9 Hoppew OrJ / ./ ./ 0 

No 10 Hopper ON / / ,/ 0 

N<D> 1 i Hopper ()tJ J j / 0 

EQUWMENTPROBLEMS _____________________________________________ ___ 

MECHANICAL WORK PERFORMED _____________________________ -,-----______ _ 

COMMENTS: 
--··.~E.. F. 

~ ·.~t·· . -~+--0 .. ~~. 

Temperf:ng Air Temp; 

lillli~t. Temperature: 

Stack Iemperature~ 

: "!"". 

"F 

;~iLiff~ IF·~.i1Hi .. 0 ;· /, }'uR i:E; :Err~[i!t} 

!BaghoMste Jmowe1 

T 11"2\!rnStfer mower. 

Air Pressure; 

.-,_ f\ D.:'B 

-- _'J:-__ ~;.L __ Jf Cj ll 

PSI -·-----·-·- --

__ LQ.o__psll 

MAGN.EHELIC GAUGES O!rn Line Cle~ming On Line CDeaJrnhng 

_:_LhaHzO 

=J_l!rnHzO 

.:_l_InH20 

. No l Hopper Pressure-\ b.S InH20 -:_ ,.6 lnH20 No 7 Hopper P~ressure __:t_l_lnH20 

No 2 Hopper Pressure ""i InH20 -:_ LinH20 No 8 Hopper Pressure _!_]_lnH20 

No 3 Hopper Pressure t b ,5 lnH20 -:: LinH20 No 9 Hopper Pressure i- 1? S InHzO 

No 4 Hopper Pressure ~InH 0 -~/ _InH20 No 10 Hopper Pressure t (lnHzO 

No 5 HopperPressmre +-~.5 InH20 ~InH 0 No il Hopper Pressure + SlnHzO 

No 6 Hopper PressruHre ~inH 0 ~lnHzO 

Screw Rotary Bags 

-:_L_InHzO 

- __l_ lnH.zO 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper OtJ ~L / / () 

No 2 Hopper Obl ./ / ./ t) 

No 3 Hopper QAl 

No 4 Hopper OtJ. 

/ / / 

j / / (J 

No 5 Hopper Q~l / I ,/ 0 

No 6 Hopper otJ ,/ ./ ./ 0 

No 7 Hopper f2iJ / I ,/ a 

No 8 Hopper OtJ ,£_ / v 

No 9 Hopper f)_tJ ,j / ./ Q 

No 10 Hopper ()JJ ,.,.,.. . 

No 11 Hopper oAJ 

/ ../ 0 

/ ./ v c 

~ B~ 

EQUWMENTPROBLEMS ________________________________________________ __ 

MECHANICAL WORK PERFORMED ________________________________________ _ 

COMMENTS: 
. . . ..:.,. ~ 

~·.oo_ B·.~.: .. ~ ..... 

9'15 IJ,tYJ·~l. 

~ I .fttL fdtLlt~~ . t4 d-.. fth.JA~Q ... t'lif~ ... __ _;··---~-L.c..DllrnPgJS. .. 

_ {:,~Q _________ .. ... 3 L{g .. .. _ ....... joQ 

. -~ :fQ ______ , .. .. ~ '1 Q fa 0 

9' :So A. ;r1. '3"10 3110 .... .. . .. . ... ---... f.:J? . 

q: '15 

to:oo 

10:15 

w·.sD 

10-45 

'! ' OD 

i i !5 

il ~0 

,I o..fS" 

!..l'Do 

\J_ \IS 

\.l$ 

:.l ...15 

J[) 

:s 

0!'... '' _._,..,., • o," • O< o '-o , •• ,_~~CO ._.,.~. ~~- AO • ~· 

A:WI· •.. -~~-Q .. -

~.trl· . 3'-{Q 

,. . rl'l· ~~----

!ll.)N\• ....... 3lf.D 

IH'VJ, 3t{Q __ 

~.M· 3'1Q 

lim· 3L[O 

I!).V"f'l, 31.40 -. .. ---

tl.W\ \ 3d..o 

{lfYI 340 .. 

fi,'N). 3YD 

f. {'II., 3Yn 

r.{f\. \)~ <·~o 

f. m. 350 

p fl'). 

3'19' 

33Q_ . 

3,0' 

3'iO 

31(0 

31./0 . ... ; j , ; 

34'7) .. 

3-i'() 

3;~.0 

3yp 

s'-(o 

3t.to 

'34fl 

345 

bO 

(:,o 

ko 

bO 

bO 

bO 

bO 

foO 

60 

bO 

ss- - ...... -----·- ··----~ ---~---~ .. . .. ' 

---- ·--~·· ~ . 

55 

ss 

. 55 

,s-5 

55 

ss 

5S 

SS' 

.5~ 

ss 

s~ 

55 

ss 
. )._. --~c ~., .... ·. 

~c:. ;: -~ _, f N'• ,1<;. 

-,'I) 

-~·\ f,fi\ 

3' -...:: -~ f.rt, 

]'WO fiY\ 

3 _S') f,'{Y· 

'-\ \0 f. 

y:JS f>.W\ -

!.\ ~0 f.M. 

r·" 

~·.5S f,f{\. 

5'10 r.1Y'. 

s·.;;ts f.t'n, ... 

S'iV f.r.-1. - .. 

.s:ss f¥~\ 

6·.ro b~l 

b ·._:1.5 f,{I)L 

~ ·.~'0 f.ri'\~ .. 

1.·· 0 ._;~ 

3'-(0 

2·'.~[) 

'2>30 

3'-ID 

.. 3'10 

J!.fD 

]d--O 

7c).__G 

.._) . .. 

-:1,30 

.. ../· .. 

330 

3~ 

?,31) 

~Ltc 

~~'0 

3Li1> 

3Yo. 

~·-tD 

3.30 

3::.0 

330 

330 

3}-o 

3d{) 

330 

j30 

33D . '. ___ .. ~---- . ....,,___ ' 

330 

i.bO 

&;,) 

f,l) -------· ,., .. 

---·- ---~ 

... --·. ---~- ... ___ .... -------------~----· ~-

bD 

bO 

bu 

,_.,_.,.. ..... ,----···•~~---·-w• 

330 

3~0 

~40 

--- _,.,,... --~--~- ----.. .. . 

.. -~- ----------------------~- -~· 

b7)' 

bl>. 

.(.,"'('' -:'"--' 

--~ -...) 

-S~_::-

--L... l .. ..._;.J 

,5" :[; 

s~ 

. -t-~ ----··-....... ____ , _______ .............. -.......... _ ..................... ---···~- --~ ---·--·-·--------------------... ··-.... ______________ ..... . 

. . -~. - ----~--~-" ------- ---~+-t -----------· . ------·--· .... - .............. ---·-···· ·---·-· -·--···-··----.. ------------··-~------------···- --- --- _ .. --· ..... ___ .....: .. -----··· .... -.. 

. ...... _ ····~------·-

\ ! ~ 

'i 

it 

~- . -~~ -.--- ..... - __ ,__ .... ---+ t· -- __ ....... ______ -----~_....,. ___ .:.---..-- ~- -· ·-

\'\ .. --··· -·----~----~~- -------~ -·· ~-----------------·----~----~--~--,._----- -~---------:-----~~-··-~· -- -~ ··-··~-------

---·· ~~- ·----·--· ~---·"'- -···---··-"--···. -- 1 ~ :\ ... --~ _______ .... --··•••'<' ••••-••l~-· ,.---. .....-••---------.o<-''~'---M•~""'' ' -~-·-------------~-~···---------.. -~-·.-·----------------------------...,-·------- ,_,, ·-· --* ______ , ' 

i \ 

_.. .. -· ·-----;·t-·-----~-----------·-: ............... ---,...-·--------·-·- ___ ........ ---·-·-----------:------~-----c....: ...... --.. ----·..;_....---..... ---·· .... ---------: 

/' 

I, I . . . ~ \ 

. ,.,'-~-

,, ' ' . ,. 

' ... \ .. ; -----"---.. ,---';._'--'--····--·· ........... ---···---------~---------------·---···· ..... --------·--------~-----:-~-~--:---~- --------------------.. --------~---

' // 

--~-~-· .""--- .............. . 

··-- ·-··- ----··--·---·· ·····. 
02ite· 

f\riTIE~ 

:;.";.' 

.. )~ -

; 

--

~~~- ~f./.~""· .. ~---~~~- ~,.-~~ () (I"· 

f;empeu·mg A.ir fr<:mtp 

Inlet Temper:atllire: 

Sta11:k Temperatitn·e "F 

Bagftn;r,il!IS£ mw,.,,.,; 

Tnl!nsfe~· Biower 

Air Pre§Sillltre __ l_Q_Q ~Si 

MAGNEHEUC GAUGES On Line Clealllling 0Jru Lim;~ 

No 1 Hopper lP'rressl!llre _:!_}_illllHzO ~llnH 0 No 7 Hopper Pressmre"+ l. 5 [nHzO 

No 2 Hopper Pressmre ~lnHzO _=_I _IIIllll(zO No 8 Hopper !P'ressunre + '}_;_5__!nH20 

No 3 Hopper Pressure ~InH 0 -=l__hnlH20 No 9Hopper Pressure -'r. *_hnH20 

No 4 Hoppe1r Pres~mJre _:!__]_inHzO --=-l_InlfzO No 10 Hopper Presslllnre +l.S InlHhO 

No 5 Hopper lP'ressmre "" 7 lnHzO 4-Inli-120 No u Hoppe1r lP'ressuwe-t 6 5InH20 

No 6 Hopper Pressure ...,. -~ inHzO - I DnllzO 

Screw Rotary Bags 

Cleaning 

__ "":'" _ _lhaHzO 

=L __ htHzO 

_:j ___ inHzO 

_-t_ _ _lnH20 

-=LlnHzO 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper atJ ,[ ~I •L 0 

No 2 Hopper QN ,I 

"' L J 0 

No 3 Hopper ()i'J .,) .I I 

No4 Hopper 0 ;,) ./ / / Q 

No 5 Hopper otJ j .,.. / / 0 

No 6Hopper OtJ / / 7 0 

No 7 Hopper O~cJ :/ __/_ / o· 

No SHopper OrJ / ./ /-

No 9Hopper nJJ ,L ./ /' a 

No 10 Hopper -OtJ ./ / / 0 

No 11 -Hopper 1>tJ / .J ./ 0 

EQUIPMENT PROBLEMS ___________ __:___ ____________ _ 

MECHANICALVVORKPERFO~ED ____________________ ___ 

COMMENTS: 
f· 

l[]ieif rempe;r2!hllre~ 

s~ad'i 1rem ij}te:rahnre: 

MA.GNEHEUC GAUGES 

No li Hopper lP'~resSI!lllfiE' _ + -Lll:!lllHlzO 

No 2 Hoppeir lP'wessll.!lire _ ~ ·:;:._ Rllll!-l{zO 

No 3 Hopper lP'n~ssttm: _ _:tlJI!lllH!20 

No 4 Hoppeir lP'iressunre "'\-- 7 ll!lllHl 20 

No 5 Hoppew lP'n:~ssil.lire ' 1 Uil1ilfllz0 

No 6 Hoppetr lP'ressl!llre _ ~.· -~ JlllliHzO 

Ollli/Off 

No 1 Hopper 0 tJ 

No 2 Hopper 0 r,J 

No 3 Hopper () ,,j 

No 4 Hoppew OtJ 

No 5 Hopper tHJ 

No 6 Hopper Ot) 

No 7 Hopper Or"' 

No 8 Hoppe• ()!\) 

No 9 Hoppew otJ 

No 10 Hoppew 0 t) 

No 1 J Hopper () ;,J 

~)J ~ . . :S-1 

l)lF 

Ch~al!llil!llg Ollll Linu~ 

--- -=--_._ :J Hil!llfhO N(J) 7 Hoppu iP'!ressill!Jne J:2il!!I]1Hh0 

~huHzO No 8 Hopper JP'neilSUi:re + 7 5 iil1lll-h0 - \ i1rnHzO --r--

-:_j__ Hll1lH20 No 9 Hopper lP'tress~W!re _ 't 7 ll:lillH20 

_:j_ __ I1111H20 No W Hoppe!r P~ressrume _:_ 7I1!11H20 

~_fti1!.H 0 No n Hopper lP'resS\lllire_ '~ ~_hlllHl"O 

=j__h11!-lhO 

Screw Ro~a:ry Bags 

· Corrnveyor Lock Chute Missillllg 

J j J 0 

/ I / 0 

.I _L_ ,} ,, I 

/ / ~ / 0 

J l / ,.,- 0 

j _L_ / _Q__ 

i L / 0 

/ f __/_ I 

j __ L_ _L_ 0 

j / / _Q__ 

/ ,/ ;/' 0 

tl!liHzO 

IlillHzO 

lii!lllHl 20 

EQUWMENTPROBLEMS ________________________________________________ __ 

.•. 

MECHANICAL WORK PERFORMED 

- COMMENTS: 
Date 

.{ 

TemjpHed;rug f'l,j,, .i:'etrifop 

Rllllie~ Tttm!Pe:rait<iill'te' 

S~:il.lck Tenmpeaa;hn:ne: 

U1Ji' 

" 

!B~gihlo~LI:ie Bk·w~! 

TlnJ\!fHife~ moweif .. 

---. + 

MAGNEHELIC GAUGES On Line Oealli!ing On Lilllle 

No 1 Hopp<elf' Plf'<essrunre -~ /2- illlli-l[zO -~-~-_l!nd·-120 No 7 Hoppeir Po·ess~tre _8__illltHzO 

/"--, 

No 2 Hoppe• P~ressuue ~illllH 0 -_j_hlllHI20 No 8 Hoppeir Pressrunre +htlf-!zO 

No 3 Hopper Pressuwe _ ~~4 iJrnH20 =-L.JI!llH20 N<O 9 !Hloppeu Pressruure r~r{/ IlllllH!zO 

No 4 HoppH Plf'essuure _·_, _inH20 ____ hnlf-!{zO No HI Hopper Pressmre_l:_:tJnlHizO N . 

--~ C:: InH20 N<O i 1 Hopper Pressru~re~\_lillllHizO 

:J_halHI20 

Screw RotaJrY Bags 

iP'§ll 

Oeamillllg 

::_l__illlllH]zO 

_,__ 

-- · !illllHI20 

~illlllHl 0 

_,_hlllHizO 

- 1 _hnlHl20 

On/Off Conve_yor Lock Chute Missing 

No 1 Hopper Ql\) ·J ./ J 

,/ 0 

No 2 Hopper ON J J ./ 0 

No 3 Hopper ON ./ J ./ 

No 4 Hopper ON / ./ / 0 

No 5 Hopper orJ / j ./ 0 

No 6 Hopper OtJ / / / 0 

No 7 Hopper -~ .J / / 0 

No 8 Hopper O!'J ./ ./ -/-

No 9 Hopper ON ./ ./ J 0 

No 10 Hoppew OfJ / ./ ~,/ D 

No 11 Hopper otJ j v' I 0 

EQUIPMENT PROBLEMS ________________________ ~ 

MECHANICAL WORK PERFORMED _____________________ _ 

COMMENTS: 

.J 
. '" 

.~~ ~ ~-- ·-~-- ' 

-~ ~t\flillplf:rmg 1\i;r Temp 

hnlet 1femperah1re: 

:Stack Temperature~ 

Ea.gh<a.;u;se BAow,~,· 

Tnvnsfe;· mower:: PS!l 

_ LCJ .... L . PSI 

MAGNEHELIC GAUGES On Line Cleaning On Line 

No l Hopper Pressure _i_llnlthO =~5 !D:llH20 No 7 Hopper Pressure ~InH 0 

No 2 Hopper Pnessullre ~inH 0 ..::::.L_InH20 No 8 Hopper Pressure _±_:::z_InHzO 

No.3 Hopper Pressure _j:_]JnHzO --=LinHzO No 9 Hoppetr Pressure _±_G_llnH20 

No 4 Hopper Pressure + ~ SinH20 _::_L lnH20 No 10 Hopper Pressmre _t~ InHzO 

No 5 Hopper lP'ressua-e _:!rl InH20 - .. S" KnH20 No u 1 Hopper Pressure ..±..h_ InHzO 

No 6 Hopper Pressure _j_2JnHzO -=-l_haHzO 

Screw Rotary Bags 

=.L_InH20 

_:-_LinH20 

_:-_/._InH20 

__ j _ _InHzO 

_-:_!_ hJtl:1l_zO 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper ON ,{_ 

• / ../ 0 

No 2 Hopper t:!JrJ / ,/ I 0 

No 3 Hopper Q/1) ,L j ./ l 

No 4Hopper ntJ / ,/ ,/ 0 

No 5 Hopper ON / ./ v 0 

No 6Hopper ON / ~ ./ 0 

No 7 Hopper Ql\} ./ ,/ ./ 0 

No SHopper QtJ / ,/ / I 

No 9Hopper o rJ / ./ /' 0 

No 10 Hopper orJ / .; / 0 

No 11 Hopper 01\J j I v' a 

~ Bfk?..s 

EQUIPMENT PROBLEMS 

MECHANICAL WORK PERFORMED ____________________ _ 

... 

, COMMENTS: