EMISSIONS TEST REPORT 

FELMAN PRODUCTION, INC. 

FURNACE #5 BAGHOUSE (ID# 001-02) 

WVDEP DAQ PERMIT # R30-0530004-2007 

PLANT ID# 03-54-05300004 

LETART, WEST VIRGINIA 

MARCH2013 

TI-1550A 

~~·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 1 

Summary of Results 1 

Discussion of Results 20 

Sampling and Analytical Procedures 22 

Sampling Location 27 

Appendixes 29 

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 2 

Table 2 Summary of Results Particulate Matter 3 

Table 2a Summary of Results Metals 4 

Table 3 Summary of Results Mercury 5 

Table 4 Dioxins/Furans/PCBs Sampling Data 6 

Table 4a Summary of Results PCBs 7 

Table 4b Summary of Results PCBs (cont.) 8 

Table 4c Summary of Results PCBs (cont.) 9 

Table 4d Summary of Results PCBs (cont.) 10 

Table 4e Summary of Results Dioxins 11 

Table 4f Summary of Results Dioxins (cont.) 12 

Table 4g Summary of Results Furans 13 

Table 4h Summary ofResults Furans (cont.) 14 

Table 5 P AHs Sampling Data 15 

Table 5a Summary ofResults PAHs 16 

Table 5b Summary of Results PAHs (cont.) 17 

Table 5c Summary ofResults PAHs (cont.) 18 

Table 5d Summary of Results PAHs (cont.) 19 
INTRODUCTION 

Emissions Test Report 

Felman Production, Inc. 

Furnace #5 Baghouse (ID#OO 1-02) 

WVDEP DAQ Permit # R30-0530004-2007 

Plant ID# 03-54-05300004 

Letart, West Virginia 

TI-1550A 

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

March 13, 14, and 15,2013, 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 #5 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 13,2013 = 4.85 tons/hr, March 14,2013 = 4.41 tons/hr, and March 15,2013 = 4.08 tons/hr. 
SUMMARY OF RESULTS 

Run Number 

Date 

Time 

Carbon Dioxide Cone. - % Vol. 

Oxygen Concentration- %Vol. 

Stack Pressure - "Hg 

Area of Stack- Sq. in. 

Volume Dry Gas Sampled - dscf 

Volume Dry Gas Sampled - dscm 

Stack Temperature- Deg. F 

Percent Moisture - % 

Velocity in the Stack - FPS 

Volumetric Flow Rate - ACFM 

Volumetric Flow Rate - DSCFM 

Isokinetic Sampling Rate - % 

Hydrogen Chloride Concentrations- ug 

Hydrogen Chloride Emissions - ug/dscm 

Hydrogen Chloride Emissions - ppm 

Hydrogen Chloride Emissions - lbs/hr 

Table 1 

HCl Sampling Data 

Baghouse #5 

1 2 

3/15/13 3/15/13 

1300 - 1535 1655 - 1905 

0.40 0.40 

20.50 20.40 

29.06 29.05 

518,400.00 518,400.00 

94.809 92.009 

2.685 2.605 

142.50 133.00 

0.77 1.07 

1.22 1.20 

263,160 261,360 

222,266 223,527 

104.3 100.6 

230.00 200.00 

85.66 76.78 

0.06 0.05 

0.0713 0.0643 

Hydrogen Chloride Emissions - lbs/ton prod. 0.017 0.016 

Production Rate (tons/hr) = 4.08 

2 

3 Average 

3/15/13 ----

1955 - 2205 ----

0.40 ----

20.40 ----

28.96 ----

518,400.00 ----

91.608 ----

2.594 ----

137.40 ----

0.92 ----

1.30 ----

275,760 ----

233,735 ----

95.8 ----

200.00 210.00 

77.10 79.85 

0.05 0.05 

0.0675 0.0677 

0.017 0.017 
SUMMARY OF RESULTS 

Table 2 

Particulate/Metals Sampling Data 

Baghouse #5 

Run Number 1 2 

Date 3/13/13 3/13/13 

Time 845 - 1300 845 - 1255 

Carbon Dioxide Cone. - % Vol. 0.30 0.30 

Oxygen Concentration - %Vol. 20.60 20.60 

Stack Pressure - "Hg 29.11 29.11 

Area of Stack - Sq. in. 518,400.00 518,400.00 

Volume Dry Gas Sampled - dscf 203.222 205.272 

Volume Dry Gas Sampled - dscm 5.755 5.813 

Stack Temperature- Deg. F 128.90 124.20 

Percent Moisture - % 0.75 0.71 

Velocity in the Stack - FPS 1.33 1.30 

Volumetric Flow Rate - ACFM 286,200 284,760 

Volumetric Flow Rate - DSCFM 247,784 248,621 

Isokinetic Sampling Rate - % 100.3 100.9 

Particulate Matter Concentrations- gr/acf 0.0003 0.0003 

Particulate Matter Concentrations- gr/dscf 0.0003 0.0004 

Particulate Matter Concentrations- ug/dscm 608.17 883.08 

Particulate Matter Emissions -lbs/hr 0.64 0.85 

Particulate Matter Emissions - lbs/ton prod. 0.13 0.18 

Production Rate (tons/hr) = 4.85 

3 

3 Average 

3/13113 ----

1410 - 1820 ----

0.30 ----

20.50 ----

29.26 ----

518,400.00 ----

201.867 ----

5.716 ----

121.60 ----

0.55 ----

1.30 ----

283,320 ----

250,152 ----

98.6 ----

0.0004 0.0003 

0.0004 0.0004 

857.24 782.83 

0.86 0.78 

0.18 0.16 
SUMMARY OF RESULTS 

Table 2a 

Particulate/Metals Sampling Data 

Baghouse #5 

Run Number 1 2 

Arsenic Concentrations - ug 2.0 2.0 

Arsenic Emissions- ug/dscm 0.35 0.34 

Arsenic Emissions - lbslhr 0.0003 0.0003 

Arsenic Emissions - lbs/ton prod. 0.0001 0.0001 

Cadmium Concentrations - ug 0.50 0.50 

Cadmium Emissions - ug/dscm 0.09 0.09 

Cadmium Emissions -lbs/hr 0.0001 0.0001 

Cadmium Emissions -lbs/ton prod. 1.66E-05 1.65E-05 

Chromium Concentrations - ug 7.40 38.30 

Chromium Emissions - ug/dscm 1.29 6.59 

Chromium Emissions - lbslhr 0.0012 0.0061 

Chromium Emissions - lbs/ton prod. 0.0002 0.0013 

Lead Concentrations- ug 25.90 36.20 

Lead Emissions- ug/dscm 4.50 6.23 

Lead Emissions - lbslhr 0.0042 0.0058 

Lead Emissions - lbs/ton prod. 0.0009 0.0012 

Manganese Concentrations - ug 607.00 547.00 

Manganese Emissions- ug/dscm 105.47 94.10 

Manganese Emissions - lbs/hr 0.0979 0.0877 

Manganese Emissions - lbs/ton prod. 0.0202 0.0181 

Nickel Concentrations - ug 5.70 14.70 

Nickel Emissions - ug/dscm 0.99 2.53 

Nickel Emissions - lbslhr 0.0009 0.0024 

Nickel Emissions - lbs/ton prod. 0.0002 0.0005 

Production Rate (tonslhr) = 4.85 

3 Average 

2.0 2.0 

0.35 0.35 

0.0003 0.0003 

0.0001 0.0001 

0.50 0.50 

0.09 0.09 

0.0001 0.0001 

1.69E-05 1.67E-05 

3.60 16.43 

0.63 2.83 

0.0006 0.0026 

0.0001 0.0005 

14.00 25.37 

2.45 4.39 

0.0023 0.0041 

0.0005 0.0008 

400.00 518.00 

69.98 89.85 

0.0656 0.0837 

0.0135 0.0173 

4.30 8.23 

0.75 1.42 

0.0007 0.0013 

0.0001 0.0003 
Vl 

SUMMARY OF RESULTS 

Time Run Trap 

945 - 1145 1 A 156021 

B 156066 

Average 

% Relative Deviation --

Time Run Trap 

1230 - 1430 2 A 156064 

B 156014 

Average 

% Relative Deviation -

Time Run Trap 

1500 - 1700 3 A 150797* 

B 156042 

Average 

%Relative Deviation 

-------------

*Spiked 

Production Rate (tonslhr) = 4.41 

Table 3 

Vapor Stage Mercury Test Results 

Baghouse 5 

Sample Sample 

Volume Volume Flow 

(1) (dscm) (dscfm) ug 

60.507 0.061 193,711 0.0013 

58.359 0.058 193,711 0.0010 

59.433 0.059 193,711 0.0011 

Sample Sample 

Volume Volume Flow 

(1) (dscm) (dscfm) ug 

53.935 0.054 192,968 0.0015 

52.617 0.053 192,968 0.0012 

53.276 0.053 192,968 0.0013 

Sample Sample 

Volume Volume Flow 

(1) (dscm) (dscfm) ug 

54.618 0.055 192,448 0.0019 

54.580 0.055 192,448 0.0011 

54.599 0.055 192,448 0.0015 

Mercury 

Emissions 

ug/dscm lbslhr lbs/ton prod. 

0.0208 1.51E-05 3.43E-06 

0.0176 1.28E-05 2.90E-06 

0.0192 1.40E-05 3.17E-06 

8.25 

Mercury 

Emissions 

ug/dscm lbslhr lbs/ton prod. 

0.0273 1.97E-05 4.47E-06 

0.0228 1.65E-05 3.74E-06 

0.0250 1.81E-05 4.10E-06 

8.89 

Mercury 

Emissions 

ug/dscm lbslhr lbs/ton prod. 

0.0355 2.56E-05 5.81E-06 

0.0198 1.43E-05 3.23E-06 

0.0277 1.99E-05 4.52E-06 

28.44 
SUMMARY OF RESULTS 

Table 4 

Dioxin/Furans/PCB's Sampling Data 

Baghouse #5 

Run Number 1 2 

Date 3/15/13 3/15/13 

Time 755 - 1010 1330- 1540 

Carbon Dioxide Cone. - % Vol. 0.40 0.40 

Oxygen Concentration - %Vol. 20.50 20.50 

Stack Pressure - "Hg 29.46 29.06 

Area of Stack- Sq. in. 518,400.00 518,400.00 

Volume Dry Gas Sampled - dscf 89.948 91.404 

Volume Dry Gas Sampled - dscm 2.547 2.588 

Stack Temperature- Deg. F 133.00 133.10 

Percent Moisture - % 0.89 0.94 

Velocity in the Stack - FPS 1.20 1.20 

Volumetric Flow Rate - ACFM 259,560 261,360 

Volumetric Flow Rate - DSCFM 225,531 223,860 

Isokinetic Sampling Rate - % 97.5 99.8 

6 

3 

3/15/13 

1700 - 1915 

0.40 

20.40 

28.96 

518,400.00 

90.311 

2.557 

152.80 

1.11 

1.20 

266,040 

219,407 

100.6 
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 #5 

1 2 

ng 5.2 8.4 

ng/dscm 2.04 3.25 

lbs/hr 1.72E-06 2.72E-06 

lbs/ton 4.23E-07 6.67E-07 

ng 0.31 0.48 

ng/dscm 0.12 0.19 

lbs/hr 1.03E-07 1.56E-07 

lbs/ton 2.52E-08 3.81E-08 

ng 5.4 8.3 

ng/dscm 2.12 3.21 

lbs/hr 1.79E-06 2.69E-06 

lbs/ton 4.39E-07 6.59E-07 

ng 0.42 0.69 

ng/dscm 0.16 0.27 

lbs/hr 1.39E-07 2.24E-07 

lbs/ton 3.41E-08 5.48E-08 

ng 15 23 

ng/dscm 5.89 8.89 

lbs/hr 4.98E-06 7.45E-06 

lbs/ton 1.22E-06 1.83E-06 

ng 0.31 0.32 

ng/dscm 0.12 0.12 

lbs/hr 1.03E-07 1.04E-07 

lbs/ton 2.52E-08 2.54E-08 

Production Rate (tons/hr) = 4.08 

3 Average 

6.6 6.7 

2.58 2.62 

2.12E-06 2.19E-06 

5.20E-07 5.37E-07 

0.42 0.40 

0.16 0.16 

1.35E-07 1.31E-07 

3.31E-08 3.21E-08 

6.2 6.6 

2.42 2.58 

1.99E-06 2.16E-06 

4.88E-07 5.29E-07 

0.51 0.54 

0.20 0.21 

1.64E-07 1.76E-07 

4.02E-08 4.30E-08 

17 18 

6.65 7.14 

5.46E-06 5.96E-06 

1.34E-06 1.46E-06 

0.34 0.32 

0.13 0.13 

1.09E-07 1.05E-07 

2.68E-08 2.58E-08 
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) 

C13-233'44'55'-HeptaCB-(189) 

Table 4b 

PCB Sampling Data 

Baghouse #5 

1 2 

ng 0.1 0.16 

ng/dscm 0.04 0.06 

lbs/hr 3.32E-08 5.18E-08 

lbs/ton 8.13E-09 1.27E-08 

ng 0.52 0.76 

ng/dscm 0.20 0.29 

lbs/hr 1.72E-07 2.46E-07 

lbs/ton 4.23E-08 6.04E-08 

ng 0.22 0.32 

ng/dscm 0.09 0.12 

lbs/hr 7.30E-08 1.04E-07 

lbs/ton 1.79E-08 2.54E-08 

ng 0.037 0.036 

ng/dscm 0.01 0.01 

lbs/hr 1.23E-08 1.17E-08 

lbs/ton 3.01E-09 2.86E-09 

ng 0.026 0.029 

ng/dscm 0.01 0.01 

lbs/hr 8.62E-09 9.40E-09 

lbs/ton 2.11E-09 2.30E-09 

ng 94 101 

ng/dscm 36.91 39.03 

lbs/hr 3.12E-05 3.27E-05 

lbs/ton 7.64E-06 8.02E-06 

Production Rate (tons/hr) = 4.08 

3 Average 

0.17 0.14 

0.07 0.06 

5.46E-08 4.66E-08 

1.34E-08 1.14E-08 

0.60 0.63 

0.23 0.24 

1.93E-07 2.04E-07 

4.73E-08 5.00E-08 

0.23 0.26 

0.09 0.10 

7.39E-08 8.35E-08 

1.81E-08 2.05E-08 

0.04 0.04 

0.02 0.01 

1.29E-08 1.23E-08 

3.15E-09 3.01E-09 

0.03 0.03 

0.01 0.01 

9.64E-09 9.22E-09 

2.36E-09 2.26E-09 

95 97 

37.15 37.70 

3.05E-05 3.15E-05 

7.48E-06 7.72E-06 
Run Number 

C 13-233'44'5-HexaCB-(156) 

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

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

C 13-23 '44'55'-HexaCB-(167) 

C 13-2344'5-PentaCB-(114) 

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

SUMMARY OF RESULTS 

Table 4c 

PCB Sampling Data 

Baghouse #5 

1 2 

ng 110 120 

ng/dscrn 43.19 46.37 

lbslhr 3.65E-05 3.89E-05 

lbs/ton 8.94E-06 9.53E-06 

ng 110 120 

ng/dscrn 43.19 46.37 

lbslhr 3.65E-05 3.89E-05 

lbs/ton 8.94E-06 9.53E-06 

ng 112 121 

ng/dscrn 43.97 46.75 

lbslhr 3.72E-05 3.92E-05 

lbs/ton 9.11E-06 9.61E-06 

ng 107 120 

ng/dscrn 42.01 46.37 

lbslhr 3.55E-05 3.89E-05 

lbs/ton 8.70E-06 9.53E-06 

ng 115 130 

ng/dscrn 45.15 50.23 

lbslhr 3.81E-05 4.21E-05 

lbs/ton 9.35E-06 1.03E-05 

ng 115 129 

ng/dscrn 45.15 49.85 

lbslhr 3.81E-05 4.18E-05 

lbs/ton 9.35E-06 1.02E-05 

Production Rate (tonslhr) = 4.08 

3 Average 

114 115 

44.58 44.71 

3.66E-05 3.73E-05 

8.98E-06 9.15E-06 

114 115 

44.58 44.71 

3.66E-05 3.73E-05 

8.98E-06 9.15E-06 

113 115 

44.19 44.97 

3.63E-05 3.76E-05 

8.90E-06 9.21E-06 

112 113 

43.80 44.06 

3.60E-05 3.68E-05 

8.82E-06 9.02E-06 

118 121 

46.15 47.18 

3.79E-05 3.94E-05 

9.30E-06 9.66E-06 

119 121 

46.54 47.18 

3.82E-05 3.94E-05 

9.37E-06 9.66E-06 
Run Number 

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

C13-33'44'55'-HexaCB-(169) 

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

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

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

SUMMARY OF RESULTS 

Table 4d 

PCB Sampling Data 

Baghouse #5 

1 2 

ng 114 129 

ng/dscm 44.76 49.85 

lbs/hr 3.78E-05 4.18E-05 

lbs/ton 9.27E-06 1.02E-05 

ng 111 113 

ng/dscm 43.58 43.66 

lbs/hr 3.68E-05 3.66E-05 

lbs/ton 9.02E-06 8.97E-06 

ng 123 136 

ng/dscm 48.29 52.55 

lbs/hr 4.08E-05 4.41E-05 

lbs/ton 1.00E-05 1.08E-05 

ng 123 137 

ng/dscm 48.29 52.94 

lbs/hr 4.08E-05 4.44E-05 

lbs/ton 1.00E-05 1.09E-05 

ng 117 127 

ng/dscm 45.94 49.07 

lbs/hr 3.88E-05 4.12E-05 

lbs/ton 9.51E-06 1.01E-05 

Production Rate (tons/hr) = 4.08 

10 

3 Average 

114 119 

44.58 46.40 

3.66E-05 3.88E-05 

8.98E-06 9.50E-06 

110 111 

43.02 43.42 

3.54E-05 3.63E-05 

8.67E-06 8.89E-06 

124 128 

48.49 49.78 

3.99E-05 4.16E-05 

9.77E-06 1.02E-05 

121 127 

47.32 49.52 

3.89E-05 4.14E-05 

9.53E-06 1.01E-05 

112 119 

43.80 46.27 

3.60E-05 3.87E-05 

8.82E-06 9.47E-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 #5 

1 2 

ng 3.5 11.9 

ng/dscm 1.37 4.60 

lbs/hr 1.16E-06 3.86E-06 

lbs/ton 2.85E-07 9.45E-07 

ng 3.5 7.8 

ng/dscm 1.37 3.01 

lbs/hr 1.16E-06 2.53E-06 

lbs/ton 2.85E-07 6.19E-07 

ng 3.2 4.5 

ng/dscm 1.26 1.74 

lbs/hr 1.06E-06 1.46E-06 

lbs/ton 2.60E-07 3.57E-07 

ng 3.1 5.6 

ng/dscm 1.22 2.16 

lbs/hr 1.03E-06 1.81E-06 

lbs/ton 2.52E-07 4.45E-07 

ng 3.2 6.0 

ng/dscm 1.26 2.32 

lbs/hr 1.06E-06 1.94E-06 

lbs/ton 2.60E-07 4.76E-07 

Production Rate (tons/hr) = 4.08 

11 

3 Average 

9.5 8.3 

3.72 3.23 

3.05E-06 2.69E-06 

7.48E-07 6.59E-07 

6.6 6.0 

2.58 2.32 

2.12E-06 1.94E-06 

5.20E-07 4.75E-07 

3.3 3.7 

1.29 1.43 

1.06E-06 1.19E-06 

2.60E-07 2.93E-07 

3.2 4.0 

1.25 1.54 

1.03E-06 1.29E-06 

2.52E-07 3.16E-07 

3.2 4.1 

1.25 1.61 

1.03E-06 1.34E-06 

2.52E-07 3.30E-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 #5 

1 2 

ng 5.2 13.7 

ng/dscm 2.04 5.29 

lbslhr 1.72E-06 4.44E-06 

lbs/ton 4.23E-07 1.09E-06 

ng 11.9 37.8 

ng/dscm 4.67 14.61 

lbslhr 3.95E-06 1.22E-05 

lbs/ton 9.68E-07 3.00E-06 

Production Rate (tonslhr) = 4.08 

12 

3 Average 

3.1 7.3 

1.21 2.85 

9.96E-07 2.39E-06 

2.44E-07 5.85E-07 

4.7 18.1 

1.84 7.04 

1.51E-06 5.90E-06 

3.70E-07 1.45E-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 #5 

1 2 

ng 220 260 

ng/dscm 86.38 100.46 

lbslhr 7.30E-05 8.42E-05 

lbs/ton 1.79E-05 2.06E-05 

ng 23.7 32.9 

ng/dscm 9.31 12.71 

lbslhr 7.86E-06 1.07E-05 

lbs/ton 1.93E-06 2.61E-06 

ng 20.6 28.7 

ng/dscm 8.09 11.09 

lbs/hr 6.83E-06 9.30E-06 

lbs/ton 1.67E-06 2.28E-06 

ng 13 20.2 

ng/dscm 5.10 7.81 

lbslhr 4.31E-06 6.55E-06 

lbs/ton 1.06E-06 1.60E-06 

ng 5.5 11.3 

ng/dscm 2.16 4.37 

lbs/hr 1.82E-06 3.66E-06 

lbs/ton 4.47E-07 8.97E-07 

Production Rate (tons/hr) = 4.08 

13 

3 Average 

460 313 

179.90 122.25 

1.48E-04 1.02E-04 

3.62E-05 2.49E-05 

46.3 34.3 

18.11 13.37 

1.49E-05 l.llE-05 

3.65E-06 2.73E-06 

38.1 29.1 

14.90 11.36 

1.22E-05 9.46E-06 

3.00E-06 2.32E-06 

26.8 20.0 

10.48 7.80 

8.61E-06 6.49E-06 

2.11E-06 1.59E-06 

13.4 10.1 

5.24 3.92 

4.31E-06 3.26E-06 

1.06E-06 8.00E-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 #5 

1 2 

ng 3.4 8.4 

ng/dscm 1.33 3.25 

lbslhr 1.13E-06 2.72E-06 

lbs/ton 2.76E-07 6.67E-07 

ng 3.8 4.8 

ng/dscm 1.49 1.85 

lbslhr 1.26E-06 1.56E-06 

lbs/ton 3.09E-07 3.81E-07 

ng 4.6 10.9 

ng/dscm 1.81 4.21 

lbslhr 1.53E-06 3.53E-06 

lbs/ton 3.74E-07 8.66E-07 

ng 3.5 3.6 

ng/dscm 1.37 1.39 

lbslhr 1.16E-06 1.17E-06 

lbs/ton 2.85E-07 2.86E-07 

ng 4.5 17.5 

ng/dscm 1.77 6.76 

lbslhr 1.49E-06 5.67E-06 

lbs/ton 3.66E-07 1.39E-06 

Production Rate (tonslhr) = 4.08 

14 

3 Average 

5.1 5.633 

1.99 2.19 

1.64E-06 1.83E-06 

4.02E-07 4.48E-07 

3.3 3.967 

1.29 1.55 

1.06E-06 1.29E-06 

2.60E-07 3.17E-07 

10.1 8.5 

3.95 3.32 

3.25E-06 2.77E-06 

7.96E-07 6.78E-07 

5 4.0 

1.96 1.57 

1.61E-06 1.31E-06 

3.94E-07 3.21E-07 

33.6 18.5 

13.14 7.22 

1.08E-05 5.99E-06 

2.65E-06 1.47E-06 
SUMMARY OF RESULTS 

Table 5 

P AH Sampling Data 

Baghouse #5 

Run Number 1 

Date 3/14/13 

Time 930 - 1145 

Carbon Dioxide Cone. - % Vol. 0.30 

Oxygen Concentration- %Vol. 20.50 

Stack Pressure - "Hg 29.46 

Area of Stack - Sq. in. 518,400.00 

Volume Dry Gas Sampled - dscf 79.204 

Volume Dry Gas Sampled - dscm 2.243 

Stack Temperature- Deg. F 117.40 

Percent Moisture - % 1.22 

Velocity in the Stack - FPS 1.01 

Volumetric Flow Rate - ACFM 217,800 

Volumetric Flow Rate - DSCFM 193,711 

Isokinetic Sampling Rate - % 100.0 

15 

2 

3/14113 

1240- 1455 

0.30 

20.60 

29.46 

518,400.00 

81.821 

2.317 

125.70 

0.84 

1.00 

219,240 

192,968 

103.7 

3 

3/14/13 

1520 - 1730 

0.40 

20.40 

29.08 

518,400.00 

76.216 

2.158 

122.20 

0.74 

1.00 

219,960 

192,448 

96.8 
Run Number 

Naphthalene 

2-Methylnaphthalene 

Acenaphthylene 

Acenaphthene 

Fluorene 

Phenanthrene 

SUMMARY OF RESULTS 

Table 5a 

PAH Sampling Data 

Baghouse #5 

1 

ng 45100 

ng/dscrn 20107.00 

lbslhr 0.0146 

lbs/ton 0.0033 

ng 19200 

ng/dscrn 8559.96 

lbslhr 0.0062 

lbs/ton 0.0014 

ng 9040 

ng/dscrn 4030.32 

lbs/hr 0.0029 

lbs/ton 0.0007 

ng 4030 

ng/dscrn 1796.70 

lbslhr 0.0013 

lbs/ton 0.0003 

ng 5080 

ng/dscrn 2264.82 

lbslhr 0.0016 

lbs/ton 0.0004 

ng 67100 

2 

28600 

12343.55 

0.0089 

0.0020 

15900 

6862.32 

0.0050 

0.0011 

4780 

2063.01 

0.0015 

0.0003 

2680 

1156.67 

0.0008 

0.0002 

2950 

1273.20 

0.0009 

0.0002 

53400 

ng/dscrn 29915.29 23047.04 

lbslhr 0.0217 0.0167 

lbs/ton 0.0049 0.0038 

Production Rate (tonslhr) = 4.41 

3 Average 

31100 34933 

14411.49 15620.68 

0.0104 0.0113 

0.0024 0.0026 

19100 18067 

8850.79 8091.02 

0.0064 0.0059 

0.0014 0.0013 

3760 5860 

1742.35 2611.89 

0.0013 0.0019 

0.0003 0.0004 

2370 3027 

1098.24 1350.54 

0.0008 0.0010 

0.0002 0.0002 

2280 3437 

1056.53 1531.52 

0.0008 0.0011 

0.0002 0.0003 

36900 52467 

17099.17 23353.83 

0.0123 0.0169 

0.0028 0.0038 
Run Number 

Anthracene 

Fluoranthene 

Pyrene 

Benzo( a )anthracene 

Chrysene 

Benzo(b )fluoranthene 

SUMMARY OF RESULTS 

Table 5b 

PAH Sampling Data 

Baghouse #5 

1 2 

ng 2170 2650 

ng/dscm 967.45 1143.72 

lbs/hr 0.0007 0.0008 

lbs/ton 0.0002 0.0002 

ng 45700 43000 

ng/dscm 20374.50 18558.48 

lbs/hr 0.0148 0.0134 

lbs/ton 0.0034 0.0030 

ng 23000 26600 

ng/dscm 10254.12 11480.36 

lbs/hr 0.0074 0.0083 

lbs/ton 0.0017 0.0019 

ng 956 466 

ng/dscm 426.21 201.12 

lbs/hr 0.0003 0.0001 

lbs/ton 7.01E-05 3.30E-05 

ng 6850 4500 

ng/dscm 3053.95 1942.17 

lbs/hr 0.0022 0.0014 

lbs/ton 0.0005 0.0003 

ng 956 466 

ng/dscm 426.21 201.12 

lbs/hr 0.0003 0.0001 

lbs/ton 7.01E-05 3.30E-05 

Production Rate (tons/hr) = 4.41 

3 Average 

1360 2060 

630.21 913.80 

0.0005 0.0007 

0.0001 0.0001 

18200 35633 

8433.73 15788.90 

0.0061 0.0114 

0.0014 0.0026 

9510 19703 

4406.86 8713.78 

0.0032 0.0063 

0.0007 0.0014 

266 563 

123.26 250.20 

0.0001 0.0002 

2.01E-05 4.11E-05 

1620 4323 

750.70 1915.60 

0.0005 0.0014 

0.0001 0.0003 

266 563 

123.26 250.20 

0.0001 0.0002 

2.01E-05 4.11E-05 
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 

P AH Sampling Data 

Baghouse #5 

1 2 

ng 344 135 

ng/dscm 153.37 58.26 

lbs/hr 1.11E-04 4.21E-05 

lbs/ton 2.52E-05 9.55E-06 

ng 1150 477 

ng/dscm 512.71 205.87 

lbs/hr 0.0004 0.0001 

lbs/ton 8.44E-05 3.37E-05 

ng 27 16 

ng/dscm 12.04 6.91 

lbs/hr 8.74E-06 4.99E-06 

lbs/ton 1.98E-06 1.13E-06 

ng 18 11 

ng/dscm 8.02 4.75 

lbs/hr 5.82E-06 3.43E-06 

lbs/ton 1.32E-06 7.78E-07 

ng 50.6 16.6 

ng/dscm 22.56 7.16 

lbs/hr 1.64E-05 5.18E-06 

lbs/ton 3.71E-06 1.17E-06 

ng 8.5 2.8 

ng/dscm 3.79 1.21 

lbs/hr 2.75E-06 8.74E-07 

lbs/ton 6.24E-07 1.98E-07 

Production Rate (tons/hr) = 4.41 

3 Average 

92.7 190.6 

42.96 84.86 

3.10E-05 6.15E-05 

7.02E-06 1.39E-05 

273 633 

126.51 281.69 

0.0001 0.0002 

2.07E-05 4.63E-05 

10 18 

4.63 7.86 

3.34E-06 5.69E-06 

7.58E-07 1.29E-06 

7.2 12.1 

3.34 5.37 

2.41E-06 3.89E-06 

5.45E-07 8.81E-07 

8 25 

3.71 11.14 

2.67E-06 8.07E-06 

6.06E-07 1.83E-06 

2 4 

0.93 1.97 

6.68E-07 1.43E-06 

1.52E-07 3.24E-07 
Run Number 

Benzo(g,h,i)perylene 

SUMMARY OF RESULTS 

ng 

Table 5d 

P AH Sampling Data 

Baghouse #5 

1 

58.9 

ng/dscm 26.26 

2 

25.2 

10.88 

lbslhr 1.91E-05 7.86E-06 

lbs/ton 4.32E-06 1.78E-06 

Production Rate (tonslhr) = 4.41 

19 

3 Average 

10.9 31.7 

5.05 14.06 

3.64E-06 1.02E-05 

8.26E-07 2.31E-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 #5 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 16.3 percent from the 

mean value of 0.92 percent. The flow rates were consistent with the largest variation being 3.19 

percent from the mean value of 226,509 DSCFM. The isokinetic sampling rates were within the 

specified limits (90 to 110 % isokinetic) with the largest variation being 4.3 percent from 100 

percent. 

Particulate/Metals 

The moisture percentages were consistent with the largest variation being 17.91 percent from the 

mean value of 0.67 percent. The flow rates were consistent with the largest variation being 0.52 

percent from the mean value of 248,852 DSCFM. The isokinetic sampling rates were within the 

specified limits (90 to 110 % isokinetic) with the largest variation being 1.4 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 13.27 percent from the 

mean value of 0.98 percent. The flow rates were consistent with the largest variation being 1.58 

percent from the mean value of 222,933 DSCFM. The isokinetic sampling rates were within the 

specified limits (90 to 110 % isokinetic) with the largest variation being 2.5 percent from 100 

percent. 

Polycyclic Aromatic Hydrocarbons (P AH) 

The moisture percentages were consistent with the largest variation being 30.71 percent from the 

mean value of 0.93 percent. The flow rates were consistent with the largest variation being 0.35 

percent from the mean value of 193,042 DSCFM. The isokinetic sampling rates were within the 

specified limits (90 to 110 % isokinetic) with the largest variation being 3.7 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 (248<>p + 

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

the sampling train contained the following impingers: 

Impinger Contents Amount 

1 0.1 N. H2S04 100 ml 

2 0.1 N. H2S04 100 ml 

3 Empty 

4 Silica Gel 400 g 

22 

Parameter 

HCl 

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<lp + 

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

the sampling train contained the following impingers: 

Im.pinger 

1 

2 

3 

4 

Contents 

5%HN03/1 O%H202 

5%HN03/l O%H202 

Empty 

Silica Gel 

Amount 

100ml 

100ml 

400g 

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-halffilter 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 (248Dp ± 

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

the sampling train contained the following impingers: 

24 
Impinger Contents 

Water-cooled condenser coil 

Water-cooled XAD-2 adsorbent tube 

1 

2 

3 

4 

Empty 

De-ionized water 

empty 

Silica Gel 

Amount 

lOOml 

400g 

Parameter 

Dioxins/Furans/PCBs 

Dioxins/Furans/PCBs 

Dioxins/Furans/PCBs 

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 (248op ± 

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

the sampling train contained the following impingers: 

25 
Im2inger 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 
N 

.....:J 

Baghouse 5 40' 

Baghouse 5 Dimensions = 40' 

Area Of Duct = 

X 90' 

518,400.0 sq. inches 

Drawings Not to Scale 

90' 

• • • • • • • 

I I I I 

i I I I ! I 

-------'-------L------~------L------~-------4---- I I I I I 

i I i 

• • • • • • • 

-------i-------~------:------~------~ _______ j ___ _ I 

• • • • • • • 

I 

: : : ; I 1 

i------~------,------~-------t-------~-------

• • • • • • • 

Traverse Feet from 

Points Stack Wall 

1 5 

2 15 

3 25 

4 35 
N 

00 

Furnace #5 Baghouse Inlet 

Gas Flow -

-

8 I 4----------------------.1~ ~ 

491" 240" 

Inside Diameter of Stack = 9 ft. 0 m. 

Port to Upstream Distance = 20 ft. 0.0 in. 

Port to Downstream Distance = 40 ft. 11.0 in. 

Area Of Stack = 9,160.9 sq. inches 

Port to Upstream Distance = 2.22 Stack Diameters 

Port to Downstream Distance = 4.55 Stack Diameters 

Drawings Not to Scale 

Traverse Percent of Inches From 

Points Diameter Stack Wall 

1 2.1 2 4/16 

2 6.7 7 4/16 

3 11.8 12 12/16 

4 17.7 19 2/16 

5 25.0 27 

6 35.5 38 5/16 

7 64.5 6911116 

8 75.0 81 

9 82.3 88 14116 

10 88.2 95 4/16 

11 93.3 100 12/16 

12 97.9 105 12116 
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 #5 

PROJECT#: TI1550 

Run Number 1 2 3 

Date 3/15/13 3/15/13 3/15/13 

Time 1300 - 1535 1655 - 1905 1955 -2205 

0 = Sample time 120 120 120 minutes 

Pb = Barometric Pressure at Port Elevation 29.05 29.05 28.95 in. Hg 

Vm =Vol. of Metered Gas- meter cond., cal corr. 96.547 95.480 93.870 cu. ft. 

Tm = Meter Temperature 64.5 74.5 65.9 Farenheit 

Tm =Meter Temperature 524.5 534.5 525.9 Rankine 

Po = Meter Orifice Pressure 1.79 1.80 1.74 in. H20 

Pma = Meter Pressure Absolute 29.18 29.18 29.08 in. Hg 

Vtwet =Sampled Gas Volume Wet 112.233 107.563 108.063 cu. ft. 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 94.809 92.009 91.608 cu.ft 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 2.685 2.605 2.594 cu. Meter 

C02 =%C02,dry 0.40 0.40 0.40 % 

02 =%02,dry 20.50 20.40 20.40 % 

co =%CO, dry 0.00 0.00 0.00 % 

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

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

Vw =Volume Water 15.6 21.1 18.1 grams 

H20 =mgas 0.77 1.07 0.92 % 

H20 = Moisture in Gas at Saturation 21.43 16.75 18.86 % 

Md =Dry Molecular Weight of Stack Gas 28.88 28.88 28.88 

Mw = Wet Molecular Weight of Stack Gas 28.80 28.76 28.78 

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

Psa = Stack Pressure, absolute 29.06 29.05 28.96 in. Hg 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #5 

PROJECT#: TI1550 

Run Number 1 2 3 

Ts =Stack Temperature 142.50 133.00 137.40 Farenheit 

Ts = Stack Temperature 334.39 329.11 331.56 Kelvin 

Ts =Stack Temperature 602.5 593 597.4 Rankine 

\I L'l P = A vg. Sum. of Pressure Square Root 0.02 0.02 0.021 

Vs = Velocity in the Stack 73.1 72.6 76.6 ft/min 

Vs = Velocity in the Stack 1.22 1.20 1.30 ft/sec 

As = Effective Stack Area 518,400.0 518,400.0 518,400.0 sq.m. 

Qa = Volumetric Flow Rate at stack cond. 263,160 261,360 275,760 acfm 

Qs = Volumetric Flow Rate, stand. cond., dry 222,266 223,527 233,735 dscfm 

IR = Isokinetic Ratio (Vn!Vs)*100 104.3 100.6 95.8 % 
TEST, Inc. I Comments: 

HCI 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 1 694.5 673.5 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 709.2 728.1 

Operator br Nozzle# %N2 79.10 3 608.4 610 

Run# 1 Nozzle Dia. (in.) 1.5 Assumed Moist % 2.00 4 900.7 916.8 

Date 3/15/13 Stack Dia.(in.) Final Moist. % 0. 77 5 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic % 104.3 6 

Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0.0015 cfm@ 11 "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 1300 982.508 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

4-6 1305 986.045 0.0004 1.70 0.759 3.0 145 264 238 67 61 59 

5 1310 990.000 0.0004 1.70 0.759 3.0 153 260 248 54 63 60 

4 1315 993.665 0.0004 1.70 0.759 3.0 135 251 250 50 64 61 

3 1320 997.455 0.0004 1.80 0.778 3.5 134 256 250 51 65 60 

2 1325 1,001.240 0.0004 1.80 0.778 3.5 140 260 250 52 65 59 

1 1330 1,005.098 0.0004 1.80 0.778 3.5 141 263 250 53 65 58 

3-6 1400 1,008.990 0.0004 1.80 0.778 3.5 112 244 250 49 67 63 

5 1405 1,013.005 0.0004 1.80 0.778 3.5 130 240 251 51 67 63 

4 1410 1,016.785 0.0004 1.80 0.778 3.5 133 259 254 52 66 61 

3 1415 1,020.305 0.0004 1.80 0.778 3.5 133 262 254 52 66 62 

2 1420 1,024.310 0.0004 1.80 0.778 3.5 134 264 249 53 68 61 

1 1425 1,028.185 0.0004 1.80 0.778 3.5 138 258 250 55 68 63 

2-6 1435 1,032.085 0.0004 1.80 0.778 3.5 144 260 252 60 66 63 

5 1440 1,036.075 0.0004 1.80 0.778 3.5 151 262 249 57 68 63 

4 1445 1,039.875 0.0004 1.80 0.778 3.5 150 259 250 51 69 63 

3 1450 1,043.650 0.0004 1.80 0.778 3.5 150 265 251 51 69 64 

2 1455 1,047.450 0.0004 1.80 0.778 3.5 149 259 250 50 70 64 

1 1500 1,051.275 0.0004 1.80 0.778 3.5 140 259 251 51 69 65 

1-6 1510 1,055.080 0.0004 1.80 0.778 3.5 169 259 255 64 66 63 

5 1515 1,058.935 0.0004 1.80 0.778 3.5 148 255 250 64 67 63 

4 1520 1,063.525 0.0004 1.80 0.778 3.5 147 256 248 62 69 64 

3 1525 1,068.430 0.0004 1.80 0.778 3.5 146 252 248 66 69 64 

2 1530 1,072.340 0.0004 1.80 0.778 3.5 147 257 249 67 69 63 

1 1535 1,076.225 0.0004 1.80 0.778 3.5 151 260 252 68 70 63 
Example Calculations 

Run Number 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 15.6 Water weight gain Ds 0 m. Stack Diameter 

Pm 1.79 "H20 Meter pressure As 518,400.0 Sq in. Stack Area 

Avg ~ P 0.000 "H20 Differential pressure Dn = 1.5 in Nozzle Diameter 

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

%C02 0.40 Carbon Dioxide %CO = 0.00 

%02 20.50 Oxygen 

Vm 93.717 acf 

Ps 0.10 "H20 

Tm 64.5 (F) 

Ts 142.5 (F) 

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

%N2 79.10 

96.547 (acf* Y) Dry Gas Volume 

29.06 "Hg Stack Pressure 

524.5 (R) Meter Temperature 

602.5 (R) Stack Temperature 

[ 1.79 ]= = 17.65 * 96.547 * _29_.0_5--=-::+:"7""::_13_._6_ 

524.5 

Vwgas = 0.0471 * Vw = 0.0471 * 15.6 = 0.7348 sft 3 

min Sample Time 

Carbon Monoxide 

Nitrogen 

94.809 sft j 

1.580 sc:fin 

Bws= Vwgas Bws* 100 = 0. 77 % Moist. Md = 28.884 

Vmstd + Vwgas 

Ts (R) 

Vs= 5129.4 * Cp * \Ps * Mw 

5129.4 * 0.84 

1-Bws = 0.9923 

* sqrt ~ P 

602.5 

29.06 * 28.800 * 

MW = 28.800 

0.020 = 73.1 fpm 1.22 

==== ===== 

ACFM= Vs *As 

144 

73.1 * 518400.0 

144 

263,160 ACFM 

fps 

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

Ts (R) * 29.92 

263,160 * 528 * 29.06 * 0.9923 

602.5 * 29.92 

222,266 DSCFM 

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

(1-Bws) * Ps * Tt * Vs * (Dn)A2 

1,039 * 94.809 * 602.5 

0.9923 * 29.06 * 120 * 73.1 * 2.25000 

104.3 % 
TEST, Inc. 

HCI Sampling Data 

Project # TI1550 

------- Plant Felman Productions LLC 

Unit/Stack Baghouse #5 

I Comments: 

Meter Box # 2010 

Meter Cal. (Y) 1.0203 

Pitot Cal. (Cp) 0.84 

---

%C02 0.40 

--- %02 20.40 

%CO --- Operator br Nozzle # %N2 79.20 --- Run# 2 Nozzle Dia. (in.) 1.5 Assumed Moist% 2.00 --- ---- Date 3/15113 Stack Dia.(in.) Final Moist.% 1.07 

---

Imp. 

1 

2 

3 

4 

5 

Sample Time 120 Static Press.("H20) Final Isokinetic% 100.6 6 -------- ---- Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0.0018 cfin@ 

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 1655 699.707 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) 

3-8 1700 703.302 0.0004 1.70 0.766 5.0 122 265 264 

7 1705 707.406 0.0004 1.80 0.786 5.0 120 255 252 

6 1710 710.804 0.0004 1.80 0.786 5.0 122 252 250 

5 1715 714.507 0.0004 1.80 0.786 5.0 120 262 252 

4 1720 718.307 0.0004 1.80 0.786 5.0 124 253 250 

3 1725 722.000 0.0004 1.80 0.786 5.0 126 249 248 

2 1730 0.308 0.0004 1.80 0.786 5.0 130 255 250 

1 1735 726.102 0.0004 1.80 0.786 5.0 131 248 250 

2-8 1745 730.004 0.0004 1.80 0.786 5.0 133 254 251 

7 1750 733.908 0.0004 1.80 0.786 5.0 134 252 251 

6 1755 737.904 0.0004 1.80 0.786 5.0 133 249 250 

5 1800 741.809 0.0004 1.80 0.786 5.0 128 249 250 

4 1805 745.804 0.0004 1.80 0.786 5.0 127 248 250 

3 1810 749.708 0.0004 1.80 0.786 5.0 132 251 250 

2 1815 753.706 0.0004 1.80 0.786 5.0 146 249 251 

1 1820 757.908 0.0004 1.80 0.786 5.0 147 249 251 

3-8 1830 761.701 0.0004 1.80 0.786 5.0 136 256 251 

7 1835 765.603 0.0004 1.80 0.786 5.0 135 250 250 

6 1840 769.508 0.0004 1.80 0.786 5.0 137 248 251 

5 1845 776.407 0.0004 1.80 0.786 5.0 140 247 248 

4 1850 781.404 0.0004 1.80 0.786 5.0 137 249 250 

3 1855 785.308 0.0004 1.80 0.786 5.0 143 249 250 

2 1900 789.303 0.0004 1.80 0.786 5.0 142 248 251 

1 1905 793.287 0.0004 1.80 0.786 5.0 146 253 250 

Initial Final 

702.7 692.1 

712.5 721.9 

611.6 614.5 

890.6 910 

10 "Hg 

10 "Hg 

Imp. Dry Gas 

Temp. Temp. 

(F) In Out 

53 79 72 

49 78 76 

483 73 71 

47 71 70 

49 72 70 

51 72 71 

51 75 73 

50 73 71 

54 76 72 

54 76 74 

56 77 76 

57 74 72 

57 72 70 

56 77 76 

62 81 80 

65 83 82 

61 76 74 

60 78 76 

60 80 78 

60 78 76 

60 72 70 

63 73 72 

63 69 67 

68 78 76 
Example Calculations 

Run Number 2 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 

Vw 21.1 Water weight gain Ds 0 

Pm 1.8 "H20 Meter pressure As 518,400.0 

Avg ~!!. P 0.000 "H20 Differential pressure On 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 

Vm 93.58 acf 

Ps 0.00 "H20 

Tm 74.5 (F) 

Ts 133.0 (F) 

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

%N2 79.20 

95.48 (acf* Y) Dry Gas Volume 

29.05 "Hg Stack Pressure 

534.5 (R) Meter Temperature 

593 (R) Stack Temperature 

~ 17.65 • 95.480 • [ 29.05 + LID! 13.6 ]= -

534.5 

Vwgas = 0.0471 * Vw = 0.0471 * 21.1 0.9938 sft 3 

Pitot Cal 

m. Stack Diameter 

Sq in. Stack Area 

m Nozzle Diameter 

min Sample Time 

Carbon Monoxide 

Nitrogen 

92.009 sft 5 

1.533 scfm 

Bws= Vwgas Bws* 100 = 1.07 % Moist. Md = 28.880 

Vmstd + Vwgas 

Vs= 5129.4 * 

5129.4 * 

Ts(R) 

\Ps * Mw 

0.84 

1-Bws = 0.9893 

* sqrt ~!!. P 

593 

29.05 * 28.764 * 

===== MW = 28.764 ===== 

0.020 = ==7=2.=6=fpm ===== 1.2 

ACFM= Vs *As 

144 

72.6 * 518400.0 

144 

261,360 ACFM 

fps 

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

Ts (R) * 29.92 

261,360 * 528 * 29.05 * 0.9893 223,527 DSCFM 

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

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

1,039 * 92.009 

0.9893 * 29.05 * 120 

593 * 29.92 

* 593 100.6 % 

* 72.6 * 2.25000 
TEST, Inc. I Comments: 

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 1 701 689.4 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 711.3 721.5 

Operator br Nozzle# %N2 79.20 3 613 615.9 

Run# 3 Nozzle Dia. (in.) 1.5 Assumed Moist % 2.00 4 910 926.6 

Date 3/15/13 Stack Dia.(in.) Final Moist. % 0.92 5 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic% 95.8 6 

Min/pt 5 Bar. Press. ("Hg) 28.95 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 1955 795.601 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

2-8 2000 799.604 0.0004 1.80 0.780 5.0 121 255 259 65 70 68 

7 2005 803.402 0.0004 1.80 0.780 5.0 120 245 250 67 69 67 

6 2010 807.305 0.0004 1.80 0.780 5.0 120 247 248 63 68 66 

5 2015 811.206 0.0004 1.80 0.780 5.0 121 251 250 58 70 68 

4 2020 815.108 0.0004 1.80 0.780 5.0 121 252 252 56 70 69 

3 2025 819.106 0.0004 1.80 0.780 5.0 120 250 249 53 69 67 

2 2030 823.007 0.0004 1.80 0.780 5.0 121 249 252 53 67 65 

1 2035 826.907 0.0004 1.80 0.780 5.0 121 253 249 56 69 67 

4-8 2045 830.902 0.0004 1.80 0.780 5.0 136 251 250 55 69 68 

7 2050 834.608 0.0004 1.80 0.780 5.0 142 251 250 56 66 64 

6 2055 838.506 0.0004 1.70 0.766 5.0 146 250 253 59 70 68 

5 2100 842.105 0.0004 1.70 0.766 5.0 147 251 250 58 67 65 

4 2105 846.002 0.0005 1.70 0.766 5.0 144 251 250 59 68 66 

3 2110 849.803 0.0005 1.70 0.766 5.0 150 250 249 57 65 63 

2 2115 853.503 0.0005 1.70 0.766 5.0 142 250 250 58 66 64 

1 2120 857.304 0.0005 1.70 0.766 5.0 143 248 251 58 64 63 

6-8 2130 861.008 0.0005 1.70 0.766 5.0 149 253 249 54 64 62 

7 2135 864.903 0.0005 1.70 0.766 5.0 150 249 250 54 63 61 

6 2140 868.705 0.0005 1.70 0.766 5.0 150 250 250 55 64 63 

5 2145 872.404 0.0005 1.70 0.766 5.0 137 251 251 58 64 62 

4 2150 876.201 0.0005 1.70 0.766 5.0 147 249 251 60 65 64 

3 2155 880.004 0.0005 1.70 0.766 5.0 150 250 249 57 66 65 

2 2200 883.806 0.0005 1.70 0.766 5.0 150 251 250 55 64 62 

1 2205 887.603 0.0005 1.70 0.766 5.0 149 250 250 55 65 63 
Example Calculations 

Run Number 3 

Ph 28.95 "Hg Barometric Pressure Cp 0.84 

Vw 18.1 Water weight gain Ds 0 

Pm 1.74 "H20 Meter pressure As 518,400.0 

Avg !J.. P 0.000 "H20 Differential pressure Dn 1.5 

Avg Sqrt !J.. P 0.021 "H20 Sqrt Diff. press. Tt 120 

%C02 0.40 Carbon Dioxide %CO 0.00 

%02 20.40 Oxygen 

Vm 92.002 acf 

Ps 0.10 "H20 

Tm 65.9 (F) 

Ts 137.4 (F) 

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

%N2 79.20 

93.87 (acf* Y) Dry Gas Volume 

28.96 "Hg Stack Pressure 

525.9 (R) Meter Temperature 

597.4 (R) Stack Temperature 

= 17.65 * 93.870 *[ 28.95 + ~ ]= 

525.9 

Vwgas = 0.0471 * Vw = 0.0471 * 18.1 0.8525 sft 3 

Pitot Cal 

in. Stack Diameter 

Sq in. Stack Area 

in Nozzle Diameter 

min Sample Time 

Carbon Monoxide 

Nitrogen 

91.608 sft j 

1.527 scfm 

Bws= Vwgas Bws* 100 = 0.92 % Moist. Md = 28.880 

Vmstd + Vwgas 

Ts (R) 

Vs=5129.4*Cp* \Ps*Mw 

5129.4 * 0.84 

==== ===== 1-Bws = 0.9908 MW = 28.780 ===== 

* sqrt !J.. P 

597.4 

28.96 * 28.780 * 0.021 ===7=6.=6=fpm 1.3 fps ===== 

ACFM= Vs *As 

144 

76.6 * 518400.0 = 275,760 ACFM 

144 

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

Ts (R) * 29.92 

275,760 * 528 * 28.96 * 0.9908 

597.4 * 29.92 

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

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

1,039 * 91.608 * 597.4 

0.9908 * 28.96 * 120 * 76.6 * 2.25000 

95.8 % 

233,735 DSCFM 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #5 

PROJECT #: TI1550 

Run Number 1 2 3 

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

Time 845 - 1300 845- 1255 1410 - 1820 

0 = Sample time 240 240 240 minutes 

Ph = Barometric Pressure at Port Elevation 29.10 29.10 29.25 in. Hg 

Vm =Vol. of Metered Gas- meter cond., cal corr. 198.921 206.331 197.059 cu. ft. 

Tm =Meter Temperature 45.4 59.2 46.5 Farenheit 

Tm =Meter Temperature 505.4 519.2 506.5 Rankine 

Po = Meter Orifice Pressure 2.09 2.25 2.00 in. H20 

Pma =Meter Pressure Absolute 29.25 29.27 29.40 in. Hg 

Vtwet =Sampled Gas Volume Wet 234.685 235.074 228.606 cu. ft. 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 203.222 205.272 201.867 cu.ft 

Vtstd = Sampled Gas Volume at Stand. Cond., dry 5.755 5.813 5.716 cu. Meter 

C02 =%C02, dry 0.30 0.30 0.30 % 

02 =% 02, dry 20.60 20.60 20.50 % 

co =%CO, dry 0.00 0.00 0.00 % 

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

EA =Excess Air 5,698.5 5,698.5 4,200.8 % 

Vw = Volume Water 32.5 31.2 23.9 grams 

H20 =mgas 0.75 0.71 0.55 % 

H20 = Moisture in Gas at Saturation 14.99 13.19 12.22 % 

Md =Dry Molecular Weight of Stack Gas 28.87 28.87 28.87 

Mw = Wet Molecular Weight of Stack Gas 28.79 28.80 28.81 

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

Psa =Stack Pressure, absolute 29.11 29.11 29.26 in. Hg 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #5 

PROJECT#: TI1550 

Run Number 

Ts =Stack Temperature 

Ts =Stack Temperature 

Ts =Stack Temperature 

\18 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 (Vn!Vs)*IOO 

Mn = Particulate Matter Catch, grams 

= Particulate Matter Catch, milligrams 

Ca = Particulate Matter Cone. - Stack Cond. 

Cs = Particulate Matter Cone. - Dry Std. Cond. 

= Particulate Matter Emissions * 

ER = Particulate Matter Emissions 

1 

128.90 

326.83 

588.9 

0.022 

79.5 

1.33 

518,400.0 

286,200 

247,784 

100.3 

0.0035 

3500.00 

0.0003 

0.0003 

608.17 

0.64 

2 3 

124.20 121.60 

324.22 322.78 

584.2 581.6 

0.022 0.022 

79.1 78.7 

1.30 1.30 

518,400.0 518,400.0 

284,760 283,320 

248,621 250,152 

100.9 98.6 

0.0051 0.0049 

5133.33 4900.00 

0.0003 0.0004 

0.0004 0.0004 

883.08 857.24 

0.85 0.86 

Farenheit 

Kelvin 

Rankine 

ft/min 

ft/sec 

sq. m. 

acfm 

dscfm 

% 

grams 

ug 

gr/acf 

gr/dscf 

ug/dscm 

lbs/hr 
TEST, Inc. ~Comments: 

Particulate/Metals Sampling Data L...----------------------l 

Project # TI1550 Meter Box# 2010 MST %C020.30 Imp. Initial Final ----- Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.60 1 716.1 681.4 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) _0_.8_4 __ %CO ----- 2 717.4 745.3 

Operator SM Nozzle # %N2 79.10 3 600.2 605 --- Run# 1 Nozzle Dia. (in.) 1.5 Assumed Moist% 1.17 4 851.3 885.8 ----- ----- Date 3/13/13 Stack Dia.(in.) Final Moist.% 0.75 5 ----- Sample Time 240 Static Press.("H20) 0.10 Final Isokinetic % 100.3 6 --- Min/pt 5 Bar. Press. ("Hg) 29.10 Initial Leak Rate 0 cfm@ 11 "Hg --- Filter# 1012 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 845 315.475 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

4-6 850 319.520 0.0005 2.10 0.832 3.5 131 258 251 66 41 41 

6 855 323.640 0.0005 2.10 0.832 3.5 132 255 252 52 44 43 

5 900 327.705 0.0005 2.10 0.832 3.5 130 256 248 54 45 44 

5 905 331.800 0.0005 2.10 0.832 3.5 135 256 245 53 46 45 

4 910 335.885 0.0005 2.10 0.832 3.5 124 258 248 54 46 46 

4 915 339.915 0.0005 2.10 0.832 3.5 120 259 250 54 47 46 

3 920 343.590 0.0005 2.10 0.832 3.5 123 259 251 57 46 45 

3 925 347.700 0.0005 2.10 0.832 3.5 118 255 248 57 46 45 

2 930 351.795 0.0005 2.10 0.832 3.5 122 254 250 58 46 46 

2 935 355.910 0.0005 2.10 0.832 3.5 122 259 252 58 46 46 

1 940 360.000 0.0005 2.10 0.832 3.5 122 255 247 59 47 46 

I 945 363.835 0.0005 2.10 0.832 3.5 127 264 251 60 47 45 

3-6 955 367.905 0.0005 2.10 0.832 3.5 126 260 249 60 45 45 

6 1000 371.820 0.0005 2.10 0.832 3.5 119 255 250 57 47 46 

5 1005 376.090 0.0005 2.10 0.832 4.0 125 254 247 59 47 46 

5 1010 380.155 0.0005 2.10 0.832 4.0 124 252 250 59 48 46 

4 1015 384.210 0.0005 2.10 0.832 4.0 126 256 248 59 45 45 

4 1020 388.250 0.0005 2.10 0.832 4.0 128 259 252 55 47 47 

3 1025 392.225 0.0005 2.10 0.832 4.0 125 265 251 58 46 46 

3 1030 396.235 0.0005 2.10 0.832 4.0 123 253 248 57 47 47 

2 1035 400.270 0.0005 2.10 0.832 4.0 127 255 250 58 47 46 

2 1040 404.325 0.0005 2.10 0.832 4.0 126 261 250 56 47 47 

1 1045 408.400 0.0005 2.10 0.832 4.0 127 261 250 54 47 47 

I 1050 412.590 0.0005 2.10 0.832 4.0 128 258 249 55 48 48 

2-6 1100 416.615 0.0005 2.10 0.832 4.0 137 256 248 52 48 47 

6 1105 420.650 0.0005 2.10 0.832 4.0 144 255 249 52 48 48 

5 IllO 424.700 0.0005 2.10 0.832 4.0 127 258 251 51 48 47 

5 1II5 428.770 0.0005 2.10 0.832 4.0 132 258 250 51 47 47 

4 1120 432.855 0.0005 2.10 0.832 4.0 147 258 255 52 47 46 

4 1125 436.925 0.0005 2.10 0.832 4.0 146 258 251 52 47 47 

3 1130 441.010 0.0005 2.10 0.832 4.0 136 265 252 52 48 47 
Example Calculations 

Run Number 1 

Ph 29.10 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 32.5 Water weight gain Ds 0 m. Stack Diameter 

Pm 2.09 "H20 Meter pressure As 518,400.0 Sq in. Stack Area 

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

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

%C02 0.30 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.60 Oxygen 

Vm 193.09 acf 

Ps 0.10 "H20 

Tm 45.4 (F) 

Ts 128.9 (F) 

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

198.921 (acf* Y) 

29.11 "Hg 

505.4 (R) 

588.9 (R) 

= 17.65 * 198.921 

%N2 79.10 Nitrogen 

Dry Gas Volume 

Stack Pressure 

Meter Temperature 

Stack Temperature 

[ 

2.09 

* 29.10 + 13.6 

505.4 J = 203.222 sft j 3.387 scfm 

Vwgas = 0.0471 * Vw = 0.0471 * 32.5 1.5308 sft 3 

Bws= Vwgas 

Vmstd + Vwgas 

Ts(R) 

Vs= 5129.4 * Cp * \Ps * Mw 

5129.4 * 0.84 

Bws*100 = 0.75 %Moist. Md = 28.872 ===== 1-Bws = 0.9925 MW = 28.790 ===== 

* sqrt 11 P 

588.9 

29.11 * 28.790 * 0.022 = 79.5 fpm 1.33 fps ==== ===== 

ACFM= Vs *As 

144 

79.5 * 518400.0 = 286,200 ACFM 

144 

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

Ts (R) * 29.92 

286,200 * 528 * 29.11 * 0.9925 

588.9 * 29.92 

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

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

1,039 * 203.222 * 588.9 

0.9925 * 29.11 * 240 * 79.5 * 2.25000 

= 100.3 % 

24 7, 784 DSCFM 
TEST, Inc. I Comments: 

Particulate/Metals Sampling Data 

Project# TI1550 Meter Box # 2010 %C020.30 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0203 %02 20.60 1 714.7 693.3 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 718.2 736.9 

Operator br Nozzle# %N2 79.10 3 622.6 627.2 

Run# 2 Nozzle Dia. (in.) 1.5 Assumed Moist % 1.80 4 890 919.3 

Date 3/13/13 Stack Dia.(in.) Final Moist.% 0.71 5 

Sample Time 240 Static Press.("H20) 0.10 Final Isokinetic % 100.9 6 

Minlpt 5 Bar. Press. ("Hg) 29.10 Initial Leak Rate 0.01 cfm@ 18 "Hg 

Filter# 1011 Leak Check Vol. Final Leak Rate 0.01 cfm@ 19 "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 845 315.581 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

7-8 850 319.805 0.0005 2.25 0.832 2.0 133 250 220 62 63 64 

8 855 324.304 0.0005 2.25 0.832 2.0 132 250 230 64 62 63 

7 900 328.505 0.0005 2.25 0.832 2.0 130 250 245 64 62 63 

7 905 332.808 0.0005 2.25 0.832 2.0 126 247 252 66 62 63 

6 910 337.203 0.0005 2.25 0.832 2.0 127 251 255 47 61 62 

6 915 341.602 0.0005 2.25 0.832 2.0 129 253 254 49 61 63 

5 920 345.902 0.0005 2.25 0.832 2.0 131 247 252 62 61 63 

5 925 350.203 0.0005 2.25 0.832 2.0 130 246 250 60 60 62 

4 930 354.601 0.0005 2.25 0.832 2.0 132 251 251 61 59 61 

4 935 359.203 0.0005 2.25 0.832 2.0 130 250 251 65 58 60 

3 940 363.506 0.0005 2.25 0.832 2.0 127 250 248 62 57 59 

3 945 367.805 0.0005 2.25 0.832 2.0 124 254 248 64 56 59 

2 950 372.203 0.0005 2.25 0.832 2.0 122 246 250 57 56 59 

2 955 376.702 0.0005 2.25 0.832 2.0 126 252 251 59 57 59 

1 1000 380.908 0.0005 2.25 0.832 2.0 127 250 252 59 57 59 

1 1005 384.704 0.0005 2.25 0.832 2.0 129 250 250 60 58 59 

6-8 1015 388.706 0.0005 2.25 0.848 2.1 126 249 231 60 59 59 

8 1020 392.607 0.0005 2.25 0.848 2.1 126 250 248 64 59 59 

7 1025 396.509 0.0005 2.25 0.848 2.1 124 250 252 66 60 60 

7 1030 400.703 0.0005 2.25 0.848 2.1 124 250 254 66 61 60 

6 1035 404.904 0.0005 2.25 0.848 2.1 122 250 251 63 62 61 

6 1040 409.108 0.0005 2.25 0.848 2.1 123 251 250 66 64 63 

5 1045 413.307 0.0005 2.25 0.848 2.1 121 248 249 66 67 64 

5 1050 417.508 0.0005 2.25 0.848 2.1 120 249 250 66 67 65 

4 1055 421.802 0.0005 2.25 0.848 2.1 122 250 250 65 68 66 

4 1100 426.108 0.0005 2.25 0.848 2.1 122 248 250 66 69 67 

3 1105 430.208 0.0005 2.25 0.848 2.1 123 251 250 66 63 67 

3 1110 434.503 0.0005 2.25 0.848 2.1 120 247 251 65 65 66 

2 1115 438.808 0.0005 2.25 0.848 2.1 121 253 247 66 62 64 

2 1120 443.105 0.0005 2.25 0.848 2.1 120 247 249 67 53 65 

1 1125 447.202 0.0005 2.25 0.848 2.1 120 250 250 67 54 66 
Example Calculations 

Run Number 2 

Ph 29.10 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 31.2 Water weight gain Ds 0 m. Stack Diameter 

Pm 2.25 "H20 Meter pressure As 518,400.0 Sq in. Stack Area 

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

Avg Sqrt L\ P 0.022 "H20 Sqrt Diff. press. Tt 240 min Sample Time 

%C02 0.30 Carbon Dioxide %CO = 0.00 Carbon Monoxide 

%02 20.60 Oxygen 

Vm 202.226 acf 

Ps 0.10 "H20 

Tm 59.2 (F) 

Ts 124.2 (F) 

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

%N2 = 79.10 

206.331 (acf* Y) Dry Gas Volume 

29.11 "Hg Stack Pressure 

519.2 (R) Meter Temperature 

584.2 (R) Stack Temperature 

~ 17.65 • 206.331 • [ 29.10 + ~ 13.6 ]--

519.2 

Nitrogen 

205.272 sft j 

3.421 scfm 

Vwgas = 0.0471 * Vw = 0.0471 * 31.2 1.4695 sft 3 

Bws= Vwgas 

Vmstd + Vwgas 

Vs = 5129.4 * 

5129.4 * 

Ts(R) 

\Ps * Mw 

0.84 

Bws*100 = 0.71 %Moist. Md = 28.872 ===== 1-Bws = 0.9929 MW = 28.795 ===== 

* sqrt L\ P 

584.2 

29.11 * 28.795 * 0.022 79.1 fpm 1.3 ==== ===== 

ACFM= Vs *As 

144 

79.1 * 518400.0 

144 

284,760 ACFM 

fps 

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

Ts (R) * 29.92 

284,760 * 528 * 29.11 * 0.9929 

584.2 * 29.92 

248,621 DSCFM 

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

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

1,039 * 205.272 * 584.2 

0.9929 * 29.11 * 240 * 79.1 * 2.25000 

100.9 % 
TEST, Inc. I Comments: 

Particulate/Metals Sampling Data 

Project# Tl1550 Meter Box# 2010 MST %C020.30 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.50 1 706.8 676 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 715.9 732.7 

Operator SM Nozzle# %N2 79.20 3 611 614.7 

Run# 3 Nozzle Dia. (in.) 1.5 Assumed Moist % 2.00 4 874.7 908.9 

Date 3/13/13 Stack Dia.(in.) 0 Final Moist. % 0.55 5 

Sample Time 240 Static Press.("H20) 0.10 Final Isokinetic % 98.6 6 

Min/pt 5 Bar. Press. ("Hg) 29.25 Initial Leak Rate 0 cfm@ 10 "Hg 

Filter# 1010 Leak Check Vol. Final Leak Rate 0 cfm@ 5 "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 1410 509.521 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

6-8 1415 513.555 0.0005 2.00 0.814 2.5 128 238 239 58 43 42 

8 1420 517.505 0.0005 2.00 0.814 2.5 126 248 249 58 44 43 

7 1425 521.435 0.0005 2.00 0.814 2.5 132 260 247 54 45 44 

7 1430 525.400 0.0005 2.00 0.814 2.5 131 258 252 54 44 44 

6 1435 529.355 0.0005 2.00 0.814 2.5 130 259 247 56 45 44 

6 1440 533.320 0.0005 2.00 0.814 2.5 131 257 248 58 45 45 

5 1445 537.300 0.0005 2.00 0.814 2.5 121 255 248 59 45 44 

5 1450 541.265 0.0005 2.00 0.814 2.5 122 259 250 60 46 44 

4 1455 545.200 0.0005 2.00 0.814 2.5 131 257 249 61 47 45 

4 1500 549.150 0.0005 2.00 0.814 2.5 144 254 248 61 46 45 

3 1505 554.510 0.0005 2.00 0.814 2.5 144 258 250 61 46 43 

3 1510 558.105 0.0005 2.00 0.814 2.5 137 255 249 61 47 45 

2 1515 562.105 0.0005 2.00 0.814 2.5 140 230 235 57 51 50 

2 1520 566.030 0.0005 2.00 0.814 2.5 138 248 247 59 52 54 

1 1525 570.080 0.0005 2.00 0.814 2.5 130 259 250 57 52 50 

1 1530 573.903 0.0005 2.00 0.814 2.5 137 259 248 59 51 49 

4-8 1540 577.900 0.0005 2.00 0.814 2.5 126 258 249 52 47 44 

8 1545 581.990 0.0005 2.00 0.814 2.5 129 258 251 51 49 47 

7 1550 585.820 0.0005 2.00 0.814 2.5 133 262 249 52 49 46 

7 1555 589.960 0.0005 2.00 0.814 2.5 136 263 250 53 50 47 

6 1600 593.706 0.0005 2.00 0.814 2.5 125 226 238 55 47 45 

6 1605 597.803 0.0005 2.00 0.814 2.5 111 270 240 54 50 48 

5 1610 601.803 0.0005 2.00 0.814 2.5 114 263 250 55 53 50 

5 1615 605.610 0.0005 2.00 0.814 2.5 119 261 251 57 51 48 

4 1620 610.504 0.0005 2.00 0.814 2.5 119 254 249 58 50 47 

4 1625 613.502 0.0005 2.00 0.814 2.5 112 262 247 57 47 45 

3 1630 617.406 0.0005 2.00 0.814 2.5 117 251 250 59 46 44 

3 1635 621.309 0.0005 2.00 0.814 2.5 111 259 248 61 46 44 

2 1640 625.202 0.0005 2.00 0.814 2.5 113 259 250 58 47 46 

2 1645 629.201 0.0005 2.00 0.814 2.5 109 262 250 57 48 45 

I 1650 633.104 0.0005 2.00 0.814 2.5 112 261 248 58 49 47 
Example Calculations 

Run Number 3 

Pb 29.25 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 23.9 Water weight gain Ds 0 10. Stack Diameter 

Pm 2 "H20 Meter pressure As 518,400.0 Sq in. Stack Area 

Avg Ll P 0.001 "H20 Differential pressure Dn 1.5 10 Nozzle Diameter 

Avg Sqrt L1 P 0.022 "H20 Sqrt Diff. press. Tt 240 m10 Sample Time 

%C02 0.30 Carbon Dioxide %CO 0.00 Carbon Monoxide 

%02 20.50 Oxygen %N2 79.20 Nitrogen 

Vm 191.282 acf 197.059 (acf* Y) Dry Gas Volume 

Ps 0.10 "H20 29.26 "Hg Stack Pressure 

Tm 46.5 (F) 506.5 (R) Meter Temperature 

Ts 121.6 (F) 581.6 (R) Stack Temperature 

17.65 * Vm * [ Pb+ I~ J • 197.059 • [ 

2.00 } Vmstd = = 17.65 29.25 + 13.6 201.867 sft j 

Tm(R) 506.5 3.364 scfm 

Vwgas = 0.0471 * Vw = 0.0471 * 23.9 1.1257 sft 3 

Bws= Vwgas 

Vmstd + Vwgas 

Ts(R) 

Vs= 5129.4 * Cp * \Ps * Mw 

5129.4 * 0.84 

Bws*100 = 0.55 %Moist. Md = 28.868 ===== 1-Bws = 0.9945 MW = 28.808 ===== 

* sqrt Ll P 

581.6 

29.26 * 28.808 * 0.022 = 78.7 fpm 1.3 

==== ===== 

ACFM= Vs *As 

144 

78.7 * 518400.0 

144 

283,320 ACFM 

fps 

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

Ts (R) * 29.92 

283,320 * 528 * 29.26 * 0.9945 250,152 DSCFM 

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

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

1,039 * 201.867 

0.9945 * 29.26 * 240 

581.6 * 29.92 

* 581.6 98.6 % 

* 78.7 * 2.25000 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #5 

PROJECT#: TI1550 

Run Number 

Date 

Time 

0 = Sample time 

Ph = 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 

3/15/13 

755 - 1010 

120 

29.45 

89.005 

56.4 

516.4 

1.60 

29.57 

103.505 

89.948 

2.547 

0.40 

20.50 

0.00 

79.10 

4,442.0 

17.2 

0.89 

16.52 

28.88 

28.79 

0.10 

29.46 

2 3 

3/15/13 3/15/13 

1330- 1540 1700 - 1915 

120 120 

29.05 28.95 

94.225 93.460 

70.9 71.2 

530.9 531.2 

1.75 1.80 

29.18 29.08 

106.702 109.487 

91.404 90.311 

2.588 2.557 

0.40 0.40 

20.50 20.40 

0.00 0.00 

79.10 79.20 

4,442.0 3,469.4 

18.5 21.5 

0.94 1.11 

16.79 27.82 

28.88 28.88 

28.78 28.76 

0.10 0.10 

29.06 28.96 

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 #5 

PROJECT#: TI1550 

Run Number 1 2 3 

Ts =Stack Temperature 133.00 133.10 152.80 Farenheit 

Ts =Stack Temperature 329.11 329.17 340.11 Kelvin 

Ts =Stack Temperature 593 593.1 612.8 Rankine 

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

Vs = Velocity in the Stack 72.1 72.6 73.9 ft/min 

Vs = Velocity in the Stack 1.20 1.20 1.20 ftlsec 

As = Effective Stack Area 518,400.0 518,400.0 518,400.0 sq.m. 

Qa = Volumetric Flow Rate at stack cond. 259,560 261,360 266,040 acfm 

Qs = Volumetric Flow Rate, stand. cond., dry 225,531 223,860 219,407 dscfm 

IR = Isokinetic Ratio (Vn/Vs)*100 97.5 99.8 100.6 % 
TEST, Inc. I Comments: Trap #7 

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 1 339.8 339.9 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 709 709.8 

Operator br Nozzle# %N2 79.10 3 622.6 623.7 

Run# 1 Nozzle Dia. (in.) 1.5 Assumed Moist % 2.00 4 906.9 922.1 

Date 3/15/13 Stack Dia.(in.) Final Moist. % 0.89 5 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic% 97.5 6 

Min/pt 5 Bar. Press. ("Hg) 29.45 Initial Leak Rate 0.002 cfm@ 10 "Hg 

Filter# ---- Leak Check Vol. Final Leak Rate 0.002 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 755 879.705 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

4-6 800 883.575 0.0004 1.60 0.737 5.0 123 252 251 68 48 47 

5 805 886.805 0.0004 1.60 0.737 5.0 127 253 250 67 51 50 

4 810 890.435 0.0004 1.60 0.737 5.0 123 263 249 64 52 50 

3 815 894.050 0.0004 1.60 0.737 5.0 120 266 249 66 53 53 

2 820 897.680 0.0004 1.60 0.737 5.0 125 257 246 68 54 53 

1 825 901.290 0.0004 1.60 0.737 5.0 133 257 250 68 56 54 

3-6 835 904.980 0.0004 1.60 0.737 5.0 126 267 251 68 49 51 

5 840 908.480 0.0004 1.60 0.737 5.0 128 255 246 68 57 55 

4 845 912.001 0.0004 1.60 0.737 5.0 129 258 253 68 57 54 

3 850 915.604 0.0004 1.60 0.737 5.0 131 263 248 67 57 55 

2 855 919.005 0.0004 1.60 0.737 5.0 124 256 253 67 54 52 

I 900 922.505 0.0004 1.60 0.737 5.0 127 258 250 39 58 56 

2-6 910 926.007 0.0004 1.60 0.737 5.0 142 254 245 43 58 55 

5 915 929.609 0.0004 1.60 0.737 5.0 128 267 248 45 61 60 

4 920 933.075 0.0004 1.60 0.737 5.0 127 263 249 46 61 59 

3 925 936.608 0.0004 1.60 0.737 5.0 131 261 248 47 61 60 

2 930 940.303 0.0004 1.60 0.737 5.0 133 260 248 49 60 57 

I 935 944.009 0.0004 1.60 0.737 5.0 153 254 257 51 61 60 

I-6 945 947.806 0.0004 1.60 0.737 5.0 147 260 254 49 60 58 

5 950 951.304 0.0004 1.60 0.737 5.0 156 256 254 49 61 60 

4 955 955.002 0.0004 1.60 0.737 5.0 138 255 247 51 61 59 

3 1000 958.709 0.0004 1.60 0.737 5.0 140 260 251 52 60 58 

2 1005 962.307 0.0004 1.60 0.737 5.0 136 270 251 51 6I 60 

1 1010 966.I01 0.0004 1.60 0.737 5.0 144 259 250 50 6I 59 
Example Calculations 

Run Number 

Pb 29.45 "Hg Barometric Pressure Cp 0.84 

Vw 17.2 Water weight gain Ds 0 

Pm 1.6 "H20 Meter pressure As 518,400.0 

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 86.396 acf 

Ps 0.10 "H20 

Tm 56.4 (F) 

Ts 133.0 (F) 

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

%N2 79.10 

89.005 (acf* Y) Dry Gas Volume 

29.46 "Hg Stack Pressure 

516.4 (R) Meter Temperature 

593 (R) Stack Temperature 

~ 17.65 • 89.005 • [ 29.45 + .LQQ 13.6 ]--

516.4 

Vwgas = 0.0471 * Vw = 0.0471 * 17.2 0.8101 sft 3 

Pitot Cal 

m. Stack Diameter 

Sq in. Stack Area 

m Nozzle Diameter 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

89.948 sft j 

1.499 scfm 

Bws= Vwgas Bws*100 = 0.89 %Moist. Md = 28.884 

Vmstd + Vwgas 

Ts(R) 

Vs=5129.4*Cp* \Ps*Mw 

1-Bws = 0.9911 

* sqrt ~ P 

===== MW = 28.787 ===== 

5129.4 * 0.84 I 593 

* \ _2_9_.4_6--*--2-8-.7-8-7 * 0.020 = 72.1 fpm 1.20 tips 

ACFM= Vs *As 

144 

72.1 * 518400.0 

144 

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

Ts (R) * 29.92 

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

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

1,039 * 89.948 

==== 

259,560 ACFM 

259,560 * 528 * 29.46 * 0.9911 

593 * 29.92 

* 593 97.5 % 

0.9911 * 29.46 * 120 * 72.1 * 2.25000 

===== 

225,531 DSCFM 
TEST, Inc. romments: Trap #8 

Dioxin!Furans/PCB's Sampling Data 

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

Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.50 1 333.1 334.2 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 696.7 696.4 

Operator br Nozzle# %N2 79.10 3 603.7 605.3 

Run# 2 Nozzle Dia. (in.) 1.5 Assumed Moist % 0.94 4 898.4 914.5 

Date 3/15/13 Stack Dia.(in.) Final Moist. % 0.94 5 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic% 99.8 6 

Min/pt 5 Bar. Press. ("Hg) 29.05 Initial Leak Rate 0.001 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 1330 607.001 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

3-8 1335 610.706 0.0004 1.70 0.766 5.0 137 248 256 67 74 73 

7 1340 614.402 0.0004 1.70 0.766 5.0 130 255 251 68 69 71 

6 1345 618.106 0.0004 1.70 0.766 5.0 136 244 250 68 71 68 

5 1350 621.708 0.0004 1.70 0.766 5.0 131 257 248 68 68 66 

4 1355 625.407 0.0004 1.70 0.766 5.0 130 253 251 60 66 64 

3 1400 629.203 0.0004 1.70 0.766 5.0 132 248 250 44 70 67 

2 1405 632.806 0.0004 1.70 0.766 5.0 132 254 251 45 73 70 

1 1410 636.465 0.0004 1.70 0.766 5.0 126 250 251 42 73 72 

2-8 1420 640.670 0.0004 1.70 0.766 5.0 120 249 252 43 72 70 

7 1425 643.809 0.0004 1.70 0.766 5.0 132 248 250 43 74 72 

6 1430 647.601 0.0004 1.70 0.766 5.0 134 250 250 53 75 74 

5 1435 651.409 0.0004 1.80 0.780 5.0 136 249 246 61 75 73 

4 1440 655.501 0.0004 1.80 0.780 5.0 134 246 248 43 75 74 

3 1445 659.608 0.0004 1.80 0.780 5.0 130 244 249 44 73 72 

2 1450 663.105 0.0004 1.80 0.780 5.0 138 254 250 44 72 70 

1 1455 667.001 0.0004 1.80 0.780 5.0 148 250 250 44 74 72 

3-8 1505 671.004 0.0004 1.80 0.780 5.0 151 248 250 46 74 73 

7 1510 674.800 0.0004 1.80 0.780 5.0 140 254 250 46 6 73 

6 1515 678.603 0.0004 1.80 0.780 5.0 134 252 255 55 75 73 

5 1520 682.509 0.0004 1.80 0.780 5.0 131 248 249 52 76 74 

4 1525 686.506 0.0004 1.80 0.780 5.0 130 245 250 51 75 74 

3 1530 690.502 0.0004 1.80 0.780 5.0 128 249 251 50 74 72 

2 1535 694.508 0.0004 1.80 0.780 5.0 130 251 247 51 77 75 

1 1540 698.464 0.0004 1.80 0.780 5.0 125 246 250 52 75 73 
Example Calculations 

Run Number 2 

Pb 29.05 "Hg Barometric Pressure Cp 0.84 

Vw 18.5 Water weight gain Ds 0 

Pm 1.75 "H20 Meter pressure As 518,400.0 

Avg !:!.. P 0.000 "H20 Differential pressure Dn 1.5 

A vg Sqrt !:!.. P 0.020 "H20 Sqrt Diff. press. Tt 120 

%C02 0.40 Carbon Dioxide %CO 0.00 

%02 20.50 Oxygen 

Vm 91.463 acf 

Ps 0.10 "H20 

Tm 70.9 (F) 

Ts 133.1 (F) 

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

%N2 79.10 

94.225 (acf* Y) Dry Gas Volume 

29.06 "Hg Stack Pressure 

530.9 (R) Meter Temperature 

593.1 (R) Stack Temperature 

~ 17.65 • 94.225 • [ 29.05 + ill 13.6 ]--

530.9 

Vwgas = 0.0471 * Vw = 0.0471 * 18.5 0.8713 sft 3 

Pitot Cal 

m. Stack Diameter 

Sq in. Stack Area 

Ill Nozzle Diameter 

min Sample Time 

Carbon Monoxide 

Nitrogen 

91.404 sft j 

1.523 scfm 

Bws= Vwgas Bws*100 = 0.94 %Moist. Md = 28.884 ==== ===== Vmstd + Vwgas 1-Bws = 0.9906 MW = 28.782 

Vs= 5129.4 * 

Ts (R) 

\Ps * Mw 

===== 

* sqrt !:!.. P 

593.1 

5129.4 * 0.84 29.06 * 28.782 * 0.020 = 72.6 fpm ===1.=2==fps 

ACFM= Vs *As 

144 

72.6 * 518400.0 

144 

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

Ts (R) * 29.92 

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

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

1,039 * 91.404 

0.9906 * 29.06 * 120 

* 

* 

==== 

261,360 ACFM 

261,360 * 528 * 29.06 * 0.9906 

593.1 * 29.92 

593.1 99.8 % 

72.6 * 2.25000 

223,860 DSCFM 
TEST, Inc. ~Comments: 

Dioxin/Furans/PCB's Sampling Data ~--------------------------------------~ 

Trap #6 

Project# TI1550 Meter Box# 2010 MST %C02 0.40 Imp. Initial Final ------ Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.40 1 340 343.6 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 721 718.6 --- ------ Operator br Nozzle # %N2 79.20 3 606.7 610.5 --- Run# 3 Nozzle Dia. (in.) 1.5 Assumed Moist% 2.00 4 922 938.5 --- ------ Date 3/15/13 Stack Dia.(in.) 0 Final Moist.% 1.11 5 ------ ------ Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic % 100.6 6 ------ Min/pt 5 Bar. Press. ("Hg) 28.95 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 Vacuo Stack Probe Filter Imp. Dry Gas 

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

Point 1700 114.158 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

2-8 1705 118.025 0.0004 1.80 0.778 5.0 151 269 249 60 69 68 

7 1710 121.850 0.0004 1.80 0.778 5.0 150 251 251 57 70 70 

6 1715 125.675 0.0004 1.80 0.778 5.0 154 259 251 59 71 68 

5 1720 129.560 0.0004 1.80 0.778 5.0 152 262 250 60 72 68 

4 1725 133.500 0.0004 1.80 0.778 5.0 163 260 250 61 71 68 

3 1730 137.175 0.0004 1.80 0.778 5.0 162 265 250 63 71 68 

2 1735 140.975 0.0004 1.80 0.778 5.0 161 265 252 63 71 68 

I 1740 144.843 0.0004 1.80 0.778 5.0 163 259 250 63 71 68 

4-8 1750 148.650 0.0004 1.80 0.778 5.0 157 267 246 64 69 68 

7 1755 152.420 0.0004 1.80 0.778 5.0 145 260 248 61 69 67 

6 1800 156.210 0.0004 1.80 0.778 5.0 157 257 250 62 69 67 

5 1805 160.100 0.0004 1.80 0.778 5.0 157 259 250 61 69 66 

4 1810 163.765 0.0004 1.80 0.778 5.5 157 260 251 63 69 68 

3 1815 167.450 0.0004 1.80 0.778 5.5 148 257 249 63 68 67 

2 1820 171.300 0.0004 1.80 0.778 5.5 157 258 249 65 67 66 

I 1825 175.078 0.0004 1.80 0.778 5.5 146 262 250 65 67 66 

2-8 1840 179.200 0.0004 1.80 0.778 5.5 150 255 248 68 71 67 

7 1845 183.135 0.0004 1.80 0.778 5.5 152 256 250 66 76 68 

6 1850 187.130 0.0004 1.80 0.778 5.5 152 258 250 57 80 71 

5 1855 191.145 0.0004 1.80 0.778 5.5 152 256 250 53 81 72 

4 1900 195.185 0.0004 1.80 0.778 5.5 135 260 249 49 83 74 

3 1905 199.250 0.0004 1.80 0.778 5.5 146 257 251 48 84 75 

2 1910 203.280 0.0004 1.80 0.778 5.5 150 258 253 44 83 77 

I 1915 204.878 0.0004 1.80 0.778 5.5 150 258 251 48 86 77 
Example Calculations 

Run Number 3 

Pb 28.95 "Hg Barometric Pressure Cp 0.84 

Vw 21.5 Water weight gain Ds 0 

Pm 1.8 "H20 Meter pressure As 518,400.0 

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 90.72 acf 93.46 (acf* Y) Dry Gas Volume 

Ps 0.10 "H20 28.96 "Hg Stack Pressure 

Tm 71.2 (F) 531.2 (R) Meter Temperature 

Ts 152.8 (F) 612.8 (R) Stack Temperature 

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

~ 17.65 • 93.460 ·[ 28.95 + ~ 13.6 ]--

531.2 

Vwgas = 0.0471 * Vw = 0.0471 * 21.5 1.0127 sft 3 

Pitot Cal 

Ill. Stack Diameter 

Sq in. Stack Area 

in Nozzle Diameter 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

90.311 sft j 

1.505 scfm 

Bws= Vwgas Bws* 100 = 1.11 % Moist. Md ==,.;2;;8;;.8,;;,80~= 

Vmstd + Vwgas 

Ts (R) 

Vs=5129.4*Cp* \Ps*Mw 

1-Bws = 0.9889 

* sqrt ~ P 

5129.4 * 0.84 I 612.8 

* \ -2-8-.9-6....::....::.=:*:..:.__2_8_. 7-5-9 * 

MW = 28.759 ===== 

0.020 = ==7=3=.9= fpm ===== 1.2 

ACFM= Vs *As 

144 

73.9 * 518400.0 

144 

266,040 ACFM 

fps 

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

Ts (R) * 29.92 

266,040 * 528 * 28.96 * 0.9889 219,407 DSCFM 

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

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

1,039 * 90.311 

0.9889 * 28.96 * 120 

612.8 * 29.92 

* 612.8 100.6 % 

* 73.9 * 2.25000 
CALCULATION SUMMARY SHEET 

PLANT: Felman Productions LLC 

UNIT: Baghouse #5 

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 

3/14/13 

930 - 1145 

120 

29.45 

78.281 

55.3 

515.3 

1.22 

29.54 

89.035 

79.204 

2.243 

0.30 

20.50 

0.00 

79.20 

4,200.8 

20.7 

1.22 

10.80 

28.87 

28.74 

0.10 

29.46 

2 3 

3/14/13 3/14/13 

1240- 1455 1520 - 1730 

120 120 

29.45 29.07 

80.024 76.032 

49.9 53.4 

509.9 513.4 

1.20 1.20 

29.54 29.16 

92.950 87.100 

81.821 76.216 

2.317 2.158 

0.30 0.40 

20.60 20.40 

0.00 0.00 

79.10 79.20 

5,698.5 3,469.4 

14.8 12.1 

0.84 0.74 

13.58 12.50 

28.87 28.88 

28.78 28.80 

0.10 0.10 

29.46 29.08 

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 #5 

PROJECT #: TI1550 

Run Number 1 2 3 

Ts =Stack Temperature 117.40 125.70 122.20 Farenheit 

Ts =Stack Temperature 320.44 325.06 323.11 Kelvin 

Ts =Stack Temperature 577.4 585.7 582.2 Rankine 

\I~ P = A vg. Sum. of Pressure Square Root 0.017 0.017 0.017 

Vs = Velocity in the Stack 60.5 60.9 61.1 ft/min 

Vs = Velocity in the Stack 1.01 1.00 1.00 ft/sec 

As = Effective Stack Area 518,400.0 518,400.0 518,400.0 sq. m. 

Qa = Volumetric Flow Rate at stack cond. 217,800 219,240 219,960 acfm 

Qs = Volumetric Flow Rate, stand. cond., dry 193,711 192,968 192,448 dscfm 

IR = Isokinetic Ratio (V niV s )* 1 00 100.0 103.7 96.8 % 
TEST, Inc. !Comments: Trap #5 pah 

P AH Sampling Data 

Project# TI1550 Meter Box # 2010 %C020.30 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0203 %02 20.50 1 333.1 333.7 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 722.8 723 

Operator br Nozzle# %N2 79.20 3 710.7 710.8 

Run# 1 Nozzle Dia. (in.) 1.5 Assumed Moist % 1.22 4 607.2 613.4 

Date 3/14/13 Stack Dia.(in.) Final Moist. % 1.22 5 902.9 916.5 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic % 100.0 6 

Min/pt 5 Bar. Press. ("Hg) 29.45 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 930 517.880 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

4-6 935 520.805 0.0003 1.10 0.614 2.5 100 253 255 67 71 64 

5 940 523.706 0.0003 1.10 0.614 2.5 106 254 253 66 70 66 

4 945 526.707 0.0003 1.10 0.614 2.5 119 250 250 66 69 67 

3 950 529.507 0.0003 1.10 0.614 2.5 110 251 251 65 65 63 

2 955 532.209 0.0003 1.10 0.614 2.5 112 250 247 63 51 48 

1 1000 534.905 0.0003 1.10 0.614 2.5 110 250 250 65 50 60 

3-6 1010 537.907 0.0003 1.10 0.614 2.5 119 250 231 59 54 51 

5 1015 540.068 0.0003 1.10 0.614 2.5 112 247 245 63 43 50 

4 1020 544.006 0.0003 1.10 0.614 2.5 105 244 251 62 48 47 

3 1025 547.108 0.0003 1.10 0.614 2.5 109 251 256 57 55 64 

2 1030 550.408 0.0003 1.30 0.687 4.0 108 251 253 65 57 66 

1 1035 554.003 0.0003 1.30 0.687 4.0 115 247 249 55 42 59 

2-6 1045 557.506 0.0003 1.30 0.687 4.0 118 252 248 66 52 59 

5 1050 560.809 0.0003 1.30 0.687 4.0 122 245 250 50 43 58 

4 1055 564.208 0.0003 1.30 0.687 4.0 126 254 252 60 45 57 

3 1100 567.602 0.0003 1.30 0.687 4.0 125 246 249 65 58 61 

2 1105 571.003 0.0003 1.30 0.687 4.0 127 247 249 66 57 61 

1 1110 574.301 0.0003 1.30 0.687 4.0 127 251 250 64 49 57 

1-6 1120 577.703 0.0003 1.30 0.687 4.0 122 251 252 61 46 57 

5 1125 581.108 0.0003 1.30 0.687 4.0 124 248 248 60 53 58 

4 1130 584.409 0.0003 1.30 0.687 4.0 125 257 251 67 47 58 

3 1135 588.209 0.0003 1.30 0.687 4.0 125 247 258 67 44 59 

2 1140 591.206 0.0003 1.30 0.687 4.0 127 256 258 66 44 57 

1 1145 594.604 0.0003 1.30 0.687 4.0 125 253 258 60 40 56 
Example Calculations 

Run Number 1 

Pb 29.45 "Hg Barometric Pressure Cp 0.84 

Vw 20.7 Water weight gain Ds 0 

Pm 1.22 "H20 Meter pressure As 518,400.0 

Avg ~ P 0.000 "H20 Differential pressure Dn 1.5 

Avg Sqrt ~ P 0.017 "H20 Sqrt Diff. press. Tt 120 

%C02 0.30 Carbon Dioxide %CO 0.00 

%02 20.50 Oxygen 

Vm 76.724 acf 

Ps 0.10 "H20 

Tm 55.3 (F) 

Ts 117.4 (F) 

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

%N2 79.20 

78.281 (acf* Y) Dry Gas Volume 

29.46 "Hg Stack Pressure 

515.3 (R) Meter Temperature 

577.4 (R) Stack Temperature 

~ 17.65 • 78.281 • [ 29.45 + w 13.6 ]--

515.3 

Vwgas = 0.0471 * Vw = 0.0471 * 20.7 0.975 sft 3 

Pitot Cal 

in. Stack Diameter 

Sq in. Stack Area 

in Nozzle Diameter 

min Sample Time 

Carbon Monoxide 

Nitrogen 

79.204 sft j 

1.320 scfm 

Bws= Vwgas Bws* 100 = 1.22 % Moist. Md = 28.868 

Vmstd + Vwgas 

Ts(R) 

Vs=5129.4*Cp* \Ps*Mw 

5129.4 * 0.84 

===== 1-Bws = 0.9878 MW = 28.735 ===== 

* sqrt ~ P 

577.4 

29.46 * 28.735 * 0.017 = ==6=0.=5 =fpm 1.01 tips ===== 

ACFM= Vs *As 

144 

60.5 * 518400.0 

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 * 79.204 

217,800 ACFM 

217,800 * 528 * 29.46 * 0.9878 

577.4 * 29.92 

* 577.4 100.0 % 

0.9878 * 29.46 * 120 * 60.5 * 2.25000 

193,711 DSCFM 
TEST, Inc. !Comments: Trap #8 

PAH Sampling Data 

Project# TI1550 Meter Box # 2010 mst %C02 0.30 Imp. Initial Final 

Plant Felman Productions LLC Meter Cal. (Y) 1.0302 %02 20.60 1 339.8 340 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 697.2 693.5 

Operator br Nozzle# %N2 79.10 3 708 705.5 

Run# 2 Nozzle Dia. (in.) 1.5 Assumed Moist % 1.80 4 609.2 609.8 

Date 3/14/13 Stack Dia.(in.) Final Moist. % 0.84 5 880.9 901.1 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic % 103.7 6 

Min/pt 5 Bar. Press. ("Hg) 29.45 Initial Leak Rate 0.001 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 1240 702.827 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

7-6 1245 707.108 0.0003 1.20 0.640 5.0 115 256 249 50 48 46 

5 1250 710.307 0.0003 1.20 0.640 5.0 117 257 251 49 49 48 

4 1255 713.204 0.0003 1.20 0.640 5.0 118 262 253 47 52 48 

3 1300 716.401 0.0003 1.20 0.640 5.0 116 259 251 47 53 49 

2 1305 719.608 0.0003 1.20 0.640 5.0 120 261 249 47 54 52 

1 1310 722.909 0.0003 1.20 0.640 5.0 122 266 250 50 53 51 

6-6 1320 726.207 0.0003 1.20 0.640 5.0 129 258 250 46 51 48 

5 1325 729.506 0.0003 1.20 0.640 5.0 128 254 248 43 52 51 

4 1330 732.707 0.0003 1.20 0.640 5.0 129 258 251 43 51 50 

3 1335 736.103 0.0003 1.20 0.640 5.0 126 263 250 43 52 50 

2 1340 739.307 0.0003 1.20 0.640 5.0 128 261 251 45 51 51 

I 1345 741.609 0.0003 1.20 0.640 5.0 129 262 254 49 51 48 

5-6 1355 744.903 0.0003 1.20 0.640 5.0 128 250 248 49 48 47 

5 1400 748.405 0.0003 1.20 0.640 5.0 129 263 251 48 49 48 

4 1405 751.704 0.0003 1.20 0.640 5.0 132 257 249 48 51 49 

3 1410 754.906 0.0003 1.20 0.640 5.0 138 260 250 51 50 49 

2 1415 758.508 0.0003 1.20 0.640 5.0 133 255 251 49 51 48 

I 1420 761.504 0.0003 1.20 0.640 5.0 117 257 257 49 51 50 

4-6 1430 764.603 0.0003 1.20 0.640 5.0 114 270 247 50 51 49 

5 1435 767.902 0.0003 1.20 0.640 5.0 126 255 245 51 47 45 

4 1440 771.008 0.0003 1.20 0.640 5.0 126 256 251 51 48 46 

3 1445 774.903 0.0003 1.20 0.640 5.0 124 258 250 52 53 51 

2 1450 777.403 0.0003 1.20 0.640 5.0 133 262 244 54 54 53 

1 1455 780.505 0.0003 1.20 0.640 5.0 140 264 248 54 50 48 
Example Calculations 

Run Number 2 

Ph 29.45 "Hg Barometric Pressure Cp 0.84 

Vw 14.8 Water weight gain Ds 0 

Pm 1.2 "H20 Meter pressure As 518,400.0 

Avg ~ P 0.000 "H20 Differential pressure Dn 1.5 

Avg Sqrt ~ P 0.017 "H20 Sqrt Diff. press. Tt 120 

%C02 0.30 Carbon Dioxide %CO 0.00 

%02 20.60 Oxygen 

Vm 77.678 acf 

Ps 0.10 "H20 

Tm 49.9 (F) 

Ts 125.7 (F) 

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

%N2 79.10 

80.024 (acf* Y) Dry Gas Volume 

29.46 "Hg Stack Pressure 

509.9 (R) Meter Temperature 

585.7 (R) Stack Temperature 

~ 17.65 • 80.024 • [ 29.45 + UQ 13.6 ]= -

509.9 

Vwgas = 0.0471 * Vw = 0.0471 * 14.8 0.6971 sft 3 

Pitot Cal 

in. Stack Diameter 

Sq in. Stack Area 

in Nozzle Diameter 

min Sample Time 

Carbon Monoxide 

Nitrogen 

81.821 sft j 

1.364 scfm 

Bws= Vwgas Bws* 100 = 0.84 % Moist. Md = 28.872 

Vmstd + Vwgas 

Vs = 5129.4 * 

5129.4 * 

Ts (R) 

\ Ps * Mw 

0.84 

==== ===== 1-Bws = 0.9916 MW = 28.781 ===== 

* sqrt ~ P 

585.7 

29.46 * 28.781 * 0.017 ===6=0.=9=fpm ===== 

ACFM= Vs *As 

144 

60.9 * 518400.0 

144 

219,240 ACFM 

fps 

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

Ts (R) * 29.92 

219,240 * 528 * 29.46 * 0.9916 

585.7 * 29.92 

192,968 DSCFM 

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

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

1,039 * 81.821 

0.9916 * 29.46 * 120 

* 585.7 103.7 % 

* 60.9 * 2.25000 
TEST, Inc. I Comments: Trap #1 

P AH 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 1 333.3 333.7 

Unit/Stack Baghouse #5 Pitot Cal. (Cp) 0.84 %CO 2 721.1 714.5 

Operator br Nozzle# %N2 79.20 3 712 710.5 

Run# 3 Nozzle Dia. (in.) 1.5 Assumed Moist% 2.00 4 608.1 611.2 

Date 3114/13 Stack Dia.(in.) 0 Final Moist.% 0.74 5 915.9 932.6 

Sample Time 120 Static Press.("H20) 0.10 Final Isokinetic% 96.8 6 

Min/pt 5 Bar. Press. ("Hg) 29.07 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 1520 781.500 ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

6-8 1525 786.407 0.0003 1.20 0.640 5.5 120 243 248 61 52 50 

7 1530 789.307 0.0003 1.20 0.640 5.5 121 254 249 66 53 52 

6 1535 792.504 0.0003 1.20 0.640 5.5 121 253 247 55 54 51 

5 1540 795.603 0.0003 1.20 0.640 5.5 120 263 249 64 54 52 

4 1545 798.804 0.0003 1.20 0.640 5.5 121 252 250 49 55 53 

3 1550 801.907 0.0003 1.20 0.640 5.5 126 261 249 49 54 52 

2 1555 805.203 0.0003 1.20 0.640 5.5 128 263 250 56 55 54 

1 1600 808.301 0.0003 1.20 0.640 5.5 124 262 249 61 57 55 

4-8 1610 810.709 0.0003 1.20 0.640 5.5 124 260 249 63 56 55 

7 1615 812.806 0.0003 1.20 0.640 5.5 123 265 249 66 55 52 

6 1620 815.304 0.0003 1.20 0.640 5.5 127 256 250 65 54 53 

5 1625 817.830 0.0003 1.20 0.640 5.5 125 257 250 67 54 51 

4 1630 820.140 0.0003 1.20 0.640 5.5 122 259 251 66 54 52 

3 1635 823.340 0.0003 1.20 0.640 5.5 123 261 249 58 54 51 

2 1640 826.550 0.0003 1.20 0.640 5.5 120 258 247 60 56 52 

1 1645 829.707 0.0003 1.20 0.640 5.5 121 262 251 62 54 51 

2-8 1655 832.904 0.0003 1.20 0.640 6.0 120 256 249 63 52 47 

7 1700 836.105 0.0003 1.20 0.640 6.0 122 260 248 66 54 53 

6 1705 839.504 0.0003 1.20 0.640 6.0 120 259 252 47 57 55 

5 1710 842.502 0.0003 1.20 0.640 6.0 120 263 257 46 54 51 

4 1715 846.004 0.0003 1.20 0.640 6.5 122 271 250 47 56 52 

3 1720 849.208 0.0003 1.20 0.640 6.5 121 256 255 46 55 54 

2 1725 852.103 0.0003 1.20 0.640 6.5 120 257 246 47 55 53 

1 1730 855.303 0.0003 1.20 0.640 6.5 122 259 249 47 54 52 
Example Calculations 

Run Number 3 

Pb 29.07 "Hg Barometric Pressure Cp 0.84 

Vw 12.1 Water weight gain Ds 0 

Pm 1.2 "H20 Meter pressure As 518,400.0 

Avg ~ P 0.000 "H20 Differential pressure Dn 1.5 

Avg Sqrt ~ P 0.017 "H20 Sqrt Diff. press. Tt 120 

%C02 0.40 Carbon Dioxide %CO 0.00 

%02 20.40 Oxygen 

Vm 73.803 acf 

Ps 0.10 "H20 

Tm 53.4 (F) 

Ts 122.2 (F) 

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

%N2 79.20 

76.032 (acf* Y) Dry Gas Volume 

29.08 "Hg Stack Pressure 

513.4 (R) Meter Temperature 

582.2 (R) Stack Temperature 

~ 17.65 • 76.032 • [ 29.07 + UQ 13.6 ]--

513.4 

Vwgas = 0.0471 * Vw = 0.0471 * 12.1 0.5699 sft 3 

Pitot Cal 

in. Stack Diameter 

Sq in. Stack Area 

in Nozzle Diameter 

min Sample Time 

Carbon Monoxide 

Nitrogen 

76.216 sft j 

1.270 scfm 

Bws= Vwgas Bws*100 = 0.74 %Moist. Md = 28.880 

Vmstd + Vwgas 

Ts(R) 

Vs= 5129.4 * Cp * \Ps * Mw 

1-Bws = 0.9926 

* sqrt ~ P 

582.2 

===== MW = 28.799 ===== 

5129.4 * 0.84 29.08 * 28.799 * 0.017 ===6=1.=1=fpm ===1===fps 

ACFM= Vs *As 

144 

61.1 * 518400.0 

144 

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

Ts (R) * 29.92 

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

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

1,039 * 76.216 

219,960 ACFM 

219,960 * 528 * 29.08 * 0.9926 

582.2 * 29.92 

* 582.2 96.8 % 

0.9926 * 29.08 * 120 * 61.1 * 2.25000 

192,448 DSCFM 
EXAMPLE CALCULATIONS 

PAH'S 

lbs/hr = __ m_,g"'--- x __ l ...... 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 

DIOXINS/FURANS AND PCB'S 

lbslhr=--m-=g- x --1-=gr"--- 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) 

lib 

x----

7,000 gr 
EXAMPLE CALCULATIONS 

MULTIPLE METALS 

lbs/hr =--m..l:::.g_ x __ l...:.gr::......__ 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) 

x---

llb 

7,000 gr 
EXAMPLE CALCULATIONS 

MERCURY 

lbslhr=--m-=g- x --1--==gr"---- 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) 

lib 

x----

7,000 gr 
EXAMPLE CALCULATIONS 

HYDROGEN CHLORIDE 

mgHCl 24.04 Hydrogen Chloride ppm= x ---

Vmstd (cu.m) 36.45 

HCllbs/hr mg HCI x __ l....!:g._r_ x DSCFM x 60 min lib 

X 

Vmstd 64.8 mg 1 hr 7,000 gr 

36.45 =Molecular Weight of Hydrogen Chloride 

24.04 = Ideal Gas Constant 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) 
--

APPENDIXB 

PRE-FLOW DATA 

,·_; 
TEST, Inc. I 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) 0.84 %CO 2 711.3 723.5 

Operator Nozzle# %N2 79.19 3 597.8 601.3 

Run # BH5 Inlet Nozzle Dia. (in.) Assumed Moist % 1.15 4 896.3 908.3 

Date 3/12/13 Stack Dia.(in.) 108 Final Moist. % 1.15 5 

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

Min/pt 5 Bar. Press. ("Hg) 29.15 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 0.23 1.20 0.628 2.0 270 42 42 

0.25 267 

0.41 266 

0.48 273 

0.48 277 

0.46 285 

0.45 290 

0.42 290 

0.40 286 

0.35 284 

0.35 275 

0.35 271 

0.23 267 

0.23 268 

0.30 260 

0.30 259 

0.30 265 

0.32 271 

0.42 280 

0.44 291 

0.45 297 

0.43 315 

0.40 310 

0.34 305 
Example Calculations 

Run Number BH5 Inlet 

Ph 29.15 "Hg Barometric Pressure Cp 0.84 

Vw 19 Water weight gain Ds 108 

Pm 1.2 "H20 Meter pressure As 9,160.9 

Avg fl. P 0.366 "H20 Differential pressure Dn 0 

A vg Sqrt fl. P 0.601 "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 42.0 (F) 

Ts 280.1 (F) 

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

Vwgas = 0.0471 * Vw = 0.0471 * 

%N2 79.19 

75.061 (acf* Y) Dry Gas Volume 

29.12 "Hg Stack Pressure 

502 (R) Meter Temperature 

740.1 (R) Stack Temperature 

[ 1.20 ]= = 17.65 * 75.061 * _29_._15 ___ + ____ 1_3._6_ 

502.0 

19 0.8949 sft 3 

Pitot Cal 

m. Stack Diameter 

Sq in. Stack Area 

in Nozzle Diameter 

mm Sample Time 

Carbon Monoxide 

Nitrogen 

77.163 sft 5 

1.286 scfm 

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

Ts(R) 

Vs=5129.4*Cp* \Ps*Mw * sqrt fl. P 

===== 

5129.4 * 0.84 I 740.1 

* \ -2-9-.1-2--*--2-8-.7-0-9 * 0.601 = 2,436.5 fpm 40.61 tips 

ACFM= Vs *As 

144 

2,436.5 * 9160.9 

144 

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

Ts (R) * 29.92 

155,004 ACFM 

155,004 * 528 * 29.12 * 0.9885 

740.1 * 29.92 

===== 

106,388 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 = 2858.685 (DSCFS) 

Eq. SD-2 Volumetric Flow Rate 

Qo = Qi+Qd 

Qo = 4631.818 (DSCFS) 

Eq. SD-1 Average Gas Velocity 

Qo v =---==--- Ao 

v= 1.286616 (FPS) 

3600}ft2 

135I(F) 595 ( R) 

45j (F) 505 ( R) 

280.1 (F) 740.1 ( R) 

106,388 (DSCFM) 1773.133 (DSCFS) 
ISOKINETIC PRELIMINARY SETUP CALCULATIONS 

%Moisture 1.15 % Y= 1.0283 

Md 0.9885 ~p = 0.000451 "H20 

C02 0.01 % \I~ p = 0.021 "H20 

02 20.80 % Pb = 29.15 "Hg 

co % Cp = 0.84 

N2 79.19 % Ts 135 OF 595 

MWd 28.834 Tm 42 OF 502 

MW 28.709 (28.966) Psa -0.400 "H20 29.12 

AssumedRm 

Assumed Tt 

Assumed cf = 

Velocity Calculation 

Vs 

\I~ 

~ 

Nozzle Diameter 

On= 

Meter Rate 

Rm 

0.850 (0.60-0.85) cfm 

240 mm 

204.0 (scfm * Tt) 

85.49 * Cp * l[t< P * \I(MW * ~:.) 

( 60.5820 * \1~ p ) = 1.2866 fps 

p = 0.02124 

p = 0.000451 

Rm * Ts * Y 

\ 0.33 * V s * Tm * Md 

Desired 1.549 in Actual 1.500 in 

0.33 * (Vs *\lAY")* Tm * Md *On 2 

Ts* Y 

0.775 cfm cf*Tt= 185.95 cf 

Correction factor = cfm = 36.482 @ 42 

\1~ p 

Rate Correction Multipliers 

Rm(new)= Tm(new) + 460 

Tm( old) + 460 

* Rm(old) 

36.482 * \I~ P ® _ ____;;4.::..2 __ 

37.209 *\I~P ® __ 5_2 __ 

37.936 * \1~ P ® __ 6_2 __ 

°FTm 

°FTm 

°FTm 

OR 

OR 

"Hg 
38.663 *\I~ p ® 72 °FTm 

39.389 * \1~ p @ 82 °FTm 

40.116 * \1~ p @ 92 °FTm 

40.843 * \1~ p @ 102 °FTm 

41.570 * \1~ p @ 112 °FTm 
TEST, Inc. ~Comments: 

Method 5D Setup ~----------------------------------------~ Project# Meter Box# 2010 MST %C02 0.01 

------ Plant Meter Cal. (Y) 1.0283 %02 20.80 

Unit/Stack Pitot Cal. (Cp) _0_.8_4 __ _ %CO ------ Operator Nozzle # %N2 79.19 ------ Run# BH5 Inlet Nozzle Dia. (in.) Assumed Moist% 1.15 ------ ------ Date 3/12/13 Stack Dia.(in.) 108 Final Moist.% 1.18 

------ Sample Time 30 Static Press.("H20) -0.40 Final Isokinetic % #REF! -------------- Min/pt 5 Bar. Press. ("Hg) 29.15 Initial Leak Rate 0.006 

Filter# Leak Check Vol. Final Leak Rate 0.006 

Dry Gas Pi tot Orifice Vacuu Stack Probe 

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

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

236.550 0.25 1.20 0.628 2.0 255 

0.23 253 

0.27 244 

0.41 242 

0.44 259 

0.46 257 

0.48 258 

0.45 255 

0.43 254 

0.37 252 

0.36 245 

0.25 244 

0.21 235 

0.24 242 

0.27 245 

0.25 249 

0.27 252 

0.28 257 

0.37 255 

0.41 260 

0.45 258 

0.45 256 

0.45 254 

0.43 244 

Imp. 

1 

2 

3 

4 

5 

6 

Initial 

703.7 

711.3 

597.8 

896.3 

Final 

695 

723.5 

601.3 

908.3 

cfm@ __ 1_4 _"Hg 

cfm@ 14 "Hg 

Filter Imp. Dry Gas 

Temp. Temp. Temp. 

(F) (F) In Out 

55 55 
Example Calculations 

Run Number BH5 Inlet 

Ph 29.15 "Hg Barometric Pressure Cp 0.84 Pitot Cal 

Vw 19 Water weight gain Ds 108 in. Stack Diameter 

Pm 1.2 "H20 Meter pressure As 9,160.9 Sq in. Stack Area 

Avg f.. P 0.353 "H20 Differential pressure Dn 0 in Nozzle Diameter 

A vg Sqrt f.. P 0.589 "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 55.0 (F) 

Ts 251.0 (F) 

Vmstd = 17.65 * Vm * [Ph+ 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 

%N2 = 79.19 

75.061 (acf* Y) Dry Gas Volume 

29.12 "Hg Stack Pressure 

515 (R) Meter Temperature 

711 (R) Stack Temperature 

~ 17.65 • 75.061 • [ 29.15 + .L2.Q 13.6 ]= -

515.0 

19 0.8949 sft 3 

Nitrogen 

75.215 sft 5 

1.254 scfm 

Bws* 100 = 1.18 % Moist. Md = 28.834 

===== 

1-Bws = 0.9882 MW = 28.706 ===== 

* sqrt f.. P 

711 

29.12 * 28.706 * 0.589 = 2,340.5 fpm 39.01 ===== 

ACFM= Vs *As 

144 

2,340.5 * 9160.9 

144 

148,896 ACFM 

fps 

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

Ts (R) * 29.92 

148,896 * 528 * 29.12 * 0.9882 106,346 DSCFM 

711 * 29.92 
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 = 2144.644 (DSCFS) 

Eq. SD-2 Volumetric Flow Rate 

Qo = Qi+Qd 

Qo = 3917.078 (DSCFS) 

Eq. SD-1 Average Gas Velocity 

Qo v = ---"'---

Ao 

v= 1.088077 (FPS) 

3600] ft2 

130) (F) 590 ( R) 

30j(F) 490 ( R) 

251 (F) 711 ( R) 

106,346 (DSCFM) 1772.433 (DSCFS) 
ISOKINETIC PRELIMINARY SETUP CALCULATIONS 

%Moisture = 

Md 

C02 

02 

co 

N2 

MWd 

MW = 

AssumedRm 

Assumed Tt = 

Assumed cf = 

Velocity Calculation 

Vs 

\I~ 

~ 

Nozzle Diameter 

Dn = 

Meter Rate 

Rm 

1.18 % Y= 1.0283 

0.9882 ~p = 0.000325 "H20 

0.01 % \1~ p = 0.018 "H20 

20.80 % Pb = 29.15 "Hg 

% Cp 0.84 

79.19 % Ts = 130 OF 590 

28.834 Tm 55 OF 515 

28.706 (28.966) Psa -0.400 "H20 29.12 

0.650 (0.60-0.85) cfm 

120 mm 

78.0 (scfm * Tt) 

85.49 * Cp * \lt. P * \I(MW *~:a) 

( 60.3304 * \1~ p ) = 1.0881 fps 

p 0.01804 

p 0.000325 

Rm * Ts * Y 

\ 0.33 * Vs * Tm * Md 

Desired 1.449 in Actual 1.500 in 

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

Ts* Y 

0.678 cfm cf* Tt = 81.32 cf 

Correction factor= cfm 

\1~ p 

37.576 @ 55 

Rate Correction Multipliers 

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

Tm( old) + 460 

37.576 *\I~ p ® 55 °FTm 

38.306 * \1~ p @ 65 °FTm 

39.035 *\I~ p ® 75 °FTm 

OR 

OR 

"Hg 
39.765 *\I~ p ® 85 °FTm 

40.495 * \1~ p @ 95 °FTm 

41.224 * \1~ p @ 105 °FTm 

41.954 * \1~ p @ 115 °FTm 

42.684 * \1~ p @ 125 °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# BH5 Inlet Nozzle Dia. (in.) Assumed Moist% 1.15 4 896.3 908.3 ----- ---- Date 3/12/13 Stack Dia.(in.) 108 Final Moist.% 1.15 5 --- Sample Time 30 Static Press.("H20) -0.40 Final Isokinetic% #REF! 6 -------- Min/pt 5 Bar. Press. ("Hg) 29.15 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 0.22 1.20 0.628 2.0 235 45 45 

0.24 232 

0.25 232 

0.30 235 

0.34 237 

0.34 245 

0.45 263 

0.45 266 

0.45 273 

0.45 274 

0.42 270 

0.45 237 

0.25 254 

0.25 255 

0.37 266 

0.42 273 

0.45 280 

0.45 281 

0.45 281 

0.45 286 

0.38 275 

0.35 271 

0.34 262 

0.32 250 
Example Calculations 

Run Number BH5 Inlet 

Pb 29.15 "Hg Barometric Pressure Cp 0.84 

Vw 19 Water weight gain Ds 108 

Pm 1.2 "H20 Meter pressure As 9,160.9 

Avg b. P 0.368 "H20 Differential pressure Dn 0 

Avg Sqrt b. P 0.603 "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 45.0 (F) 

Ts 259.7 (F) 

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

Vwgas = 0.0471 * Vw = 0.0471 * 

%N2 79.19 

75.061 (acf* Y) Dry Gas Volume 

29.12 "Hg Stack Pressure 

505 (R) Meter Temperature 

719.7 (R) Stack Temperature 

[ 1.20 ]= = 17.65 * 75.061 * _29_.1_5--::-::+:"::""7_13_._6_ 

505.0 

19 0.8949 sft 3 

Pitot Cal 

in. Stack Diameter 

Sq in. Stack Area 

in Nozzle Diameter 

min Sample Time 

Carbon Monoxide 

Nitrogen 

76.704 sft j 

1.278 scfm 

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

Ts(R) 

Vs=5129.4*Cp* \Ps*Mw * sqrt b. P 

===== 

5129.4 * 0.84 I 719.7 

* \ -2-9-.1-2--*--2-8-. 7-0-9 * 0.603 = 2,410.7 fpm 40.18 fips 

ACFM= Vs *As 

144 

2,410.7 * 9160.9 

144 

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

Ts (R) * 29.92 

153,362 ACFM 

153,362 * 528 * 29.12 * 0.9885 

719.7 * 29.92 

===== 

108,245 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. 5D-3 Dilution Air Flow Rate 

Qd = Qi (Ti-To) 

To-Tamb 

Qd = 2463.049 (DSCFS) 

Eq. 5D-2 Volumetric Flow Rate 

Qo = Qi+Qd 

Qo = 4267.132 (DSCFS) 

Eq. 5D-1 Average Gas Velocity 

Qo v = _ _;:::,__ 

Ao 

v= 1.185314 (FPS) 

3600)ft2 

130I(F) 590 ( R) 

35l (F) 495 ( R) 

259.7 (F) 719.7(R) 

108,245 (DSCFM) 1804.083 (DSCFS) 
ISOKINETIC PRELIMINARY SETUP CALCULATIONS 

%Moisture 1.15 % Y= 1.0283 

Md 0.9885 ~p = 0.000386 "H20 

C02 = 0.01 % \1~ p = 0.020 "H20 

02 = 20.80 % Pb = 29.15 "Hg 

co = % Cp 0.84 

N2 = 79.19 % Ts = 130 OF 590 

MWd 28.834 Tm 45 OF 505 

MW 28.709 (28.966) Psa = -0.400 "H20 29.12 

AssumedRm = 

Assumed Tt = 

Assumed cf = 

Velocity Calculation 

Vs 

\I~ 

~ 

Nozzle Diameter 

Dn = 

Meter Rate 

Rm 

0.650 (0.60-0.85) cfm 

120 min 

78.0 (scfm * Tt) 

85.49 • cp • lit. P • \I(Mw • ~':al 

( 60.3270 *'I~ p) = 1.1853 fps 

p = 0.01965 

p 0.000386 

Rm * Ts * Y 

\ 0.33 * Vs * Tm * Md 

Desired 1.401 in Actual 1.500 in 

0.33 * (Vs * \[A"P") * Tm * Md * Dn 2 

Ts* Y 

0.724 cfm cf * Tt = 86.90 cf 

Correction factor = cfm = 36.856 @ 45 

\1~ p 

Rate Correction Multipliers 

Rm(new)= Tm(new) + 460 

Tm( old) + 460 

* Rm(old) 

36.856 * ,,~ p @ __ 4_5 --

37.585 *\I~P ® __ 5_5 __ 

38.315 * ,,~ p @ __ 6_5 --

°FTm 

°FTm 

°FTm 

OR 

OR 

"Hg 
39.045 *\I~ p ® 75 °FTm 

39.775 * \1~ p @ 85 °FTm 

40.505 * \1~ p @ 95 °FTm 

41.235 * \1~ p @ 105 °FTm 

41.964 * \1~ p @ 115 °FTm 
APPENDIXC 

ANALYTICAL DATA 

.:~_ 

:.:.-
Run 

Number 

1 

2 

3 

ANALYTICAL RESULTS 

Filter 

Number 

1012 

1011 

1010 

Particulate Matter 

Felman Productions LLC 

Baghouse #5 

Filter Acetone Rinse 

Final Weight Final Weight 

(grams) (grams) 

0.0025 0.0010 

0.0029 0.0022 

0.0033 0.0016 

Total 

Particulate 

Matter 

(grams) 

0.0035 

0.0051 

0.0049 
' Lab Conditions ~ ·:-~ -· .. ·-. pc.. ,.,_, ,; ·~ '• ,; 0 .-,: • 

Filter Gravimetric Analysis Temperature: 18 oc 

Bar. Press.: 29.03 "Hg 

Project Number: TI1550 Location: Baghouse #5 

Company: Felman Productions LLC EPA Method: 5 Analyst: JPS 

Initial Tray Filter Tare Tray/Filter 

Weight Weight Weight Weight Results 

Filter Number: 1012 Number Date Time (g} (g} (g} (g} 

Notes: 1 4115/2013 800 0.9230 0.5504 1.4759 0.0025 

2 4/15/2013 1200 0.9230 0.5504 1.4759 0.0025 

3 4115/2013 1600 0.9230 0.5504 1.4759 0.0025 

Final Weight: 0.0025 

Initial Tray Filter Tare Tray/Filter 

Weight Weight Weight Weight Results 

Filter Number: 1011 Number Date Time (g} (g} (g} (g} 

Notes: 1 4/15/2013 800 0.9230 0.5482 1.4742 0.0030 

2 4/15/2013 1200 0.9230 0.5482 1.4742 0.0030 

3 4115/2013 1600 0.9230 0.5482 1.474 0.0028 

Final Weight: 0.0029 

Initial Tray Filter Tare Tray/Filter 

Weight Weight Weight Weight Results 

Filter Number: 1010 Number Date Time (g} (g} (g} (g} 

Notes: 1 4/15/2013 800 0.9230 0.5438 1.4701 0.0033 

2 4115/2013 1200 0.9230 0.5438 1.4701 0.0033 

3 4115/2013 1600 0.9230 0.5438 1.4701 0.0033 - Final Weight: 0.0033 
:_~. T, Inc. 

Rinse Gravimetric Analysis 

Project Number: TI1550 Lab Conditions ----------------

Company: Felman Productions LLC Temperature: 18 oc ------------

Location: Baghouse #5 Bar. Press.: 29.03 "Hg 

Analyst: JPS 

----------------

Initial Beaker Beaker/Sample Final 

Filter Beaker Weight Weight Weight 

Number Number Date Time {g} {g} {g} 

1012 5-1 4/15/2013 800 108.0241 108.0251 0.0010 

1011 5-2 4/15/2013 800 102.2316 102.2338 0.0022 

1010 5-3 4/15/2013 800 105.3084 105.31 0.0016 
Ma~am 

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 

Date Date 

Quantity Extracted Analyzed Laboratory Method 

8 2013/04/12 2013/04/12 BRL SOP-00108 

8 N/A 2013/04/12 

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

Encryption Key Ancy Sebastian 

vlt};lia£ ;,v- 18 Apr 2013 11:13:25 -04:00 

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 of? 

\i~a:o:nrn /•,nalyt!GS !mernational Gorporat!on o.:a Maxxam Anatytics 6740 Campobello Roa(J, MISS!SSauga, Ontario, L51\l 2L8 Tel: (905) 817-5700 Toll-free: 300-563-6266 Fax: {905) 817-5777 -.·1\vv-;.maxxam.ca 
Ma?§Zam 

Maxxam Job #: 8351189 

Report Date: 2013/04/18 

Maxxam ID 

~ampling Date 

roc 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 IBLANK-H2S04-M26A ~LANK-H20-M26A RUN RUN RDL pc 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 pc 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 

Page2of7 

''.lla'<x;trn /-mc1lyllcs lrnernational COrporation o!a Maxxam Analytics 6740 Campobello Roacl, MCSS.issauga, Ontario, LSN 2l8 Tel: (905) 817~5700 Toii~Free: 800~563-6266 Fax: (905) 817-5777 \'V\VW.maxxam.~ 
Ma?§l.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 

IC/SPEC 3179677 2013/04/12 

3179578 N/A 

Maxxam ID RC1307 Collected 2013/03/27 

Sample ID BLANK-H20-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 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 

IC/SPEC 3179677 2013/04/12 

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 Ana zed Anal st 

IC/SPEC 3179677 2013/04/12 2013/04/12 Ann-Marie Stern 

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 Anal zed Anal st 

IC/SPEC 3179677 2013/04/12 2013/04/12 Ann-Marie Stern 

3179578 N/A 2013/04/12 

Page 3 of7 

!Vlaxxam 1\nalvucs International COrporation o/a Maxxam Analylics 6740 Campobello Road, MlsSJssauga, Ontano, LSN 21...8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 WWV'I.maxxam.t.a 
Ma?§l.am 

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 

Instrumentation 

IC/SPEC 

Instrumentation 

IC/SPEC 

Instrumentation 

IC/SPEC 

Test Summary 

Batch Extracted 

3179677 2013/04/12 

3179578 N/A 

Batch Extracted 

3179677 2013/04/12 

3179578 N/A 

Batch Extracted 

3179677 2013/04/12 

3179578 N/A 

Page4of7 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

MauamllnalyUcs lrnernational COrporatiOn o/a Maxxam Analytics 6740 Campobello Road, Mlssissauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: BOQ-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Mar;52am 

Maxxam Job #: 8351189 

Report Date: 2013/04/18 

Results relate only to the items tested. 

Keika Ventures 

Client Project #: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O.#: 10244 

GENERAL COMMENTS 

Page 5of7 

IVla•xam Analylics ltnernational COrporation ola Maxxam Analy1ics 6740 Campobello Road, Mlssissauga, Ontario, L5N 21.8 Tel: (905) 817-5700 Toll-Free: BOQ-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma?§i.am 

QA/QC 

Batch 

Num lnit QCTvoe Parameter 

3179677 A_S Matrix Spike 

(RC1308) Hydrochloric Acid 

Spiked Blank Hydrochloric Acid 

Method Blank Hydrochloric Acid 

RPDSample/Sample 

Dup 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 

YYW/mm/dd 

2013/04/12 

2013/04/12 

2013/04/12 

2013/04/12 

Value %Recovery 

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 6of7 

1\ita'(xam /\nalylJCS lrnernaUonal CorporatiOn o!a Maxxam Anal~ltics 6740 Campobello Road, Mfssissauga, Onlarlo,l5N 2L8 Tel: (905) 817-5700 Toll-Free: 80Q-563-6266 Fax: (905) 817-5777 W\Vw.maxxam.ca 
Ma?:{Jam 

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 7 of7 

Ma.<xam Analylics Jrnernational Corporation o/a Maxxam Analytics 6740 Campobello Road, Mlssissauga, Ontano, L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ua 
Ma({52am 

Your P.O.#: 10244 

Your Project #: Tl1550 

Attention: Lorri L White 

Keika Ventures 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Chapel Hill 

101 Strangford Lane 

Durham, NC 

USA 27713 

Report Date: 2013/04/17 

MAXXAM JOB#: 8351214 

Received: 2013/04/06, 13:00 

Sample Matrix: Stack Sampling Train 

# Samples Received: 7 

CERTIFICATE OF ANALYSIS 

Date Date 

Analyses Quantity Extracted Analyzed Laboratory Method 

Metals in Combined Train (6020) 7 2013/04/10 2013/04/12 BRL SOP-00103/ BRL 

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

Encryption Key[~~~ ,1/ Ancy Sebastian 

Vfll~l)al,w- 17 Apr 201314:33:19-04:00 

Please direct all qu ""u"" '"'Ha'u"'H"";:; Certificate of Analysis to your Project Manager. 

Ancy Sebastian, C. Tech., Senior Project Manager, Air Taxies 

Email: ASebastian@maxxam.ca 

Phone# (905) 817-5831 

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

SOP-00102 

Method 

Reference 

EPA 6020 I M29 

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 8 

!V1;n:.:xam/\na!vtJc-s lrrrernalional Corporation o/a Maxxam Analy1ics 6740 campobello Road, Mlssissauga, Onlano, L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-553-6266 Fax: (905) 817'-5? 17 \'VWw.m.:co•am.t,;a 
M ({)2am 

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 pc 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 of 8 

pc Batch 

3177251 

3177251 

3177251 

3177251 

3177251 

3177251 

'Vt::n :.;;;In /•.nc-l!VUCS lmPrnatlonal Corporal!on o:a Maxxam AmlytJcs 6140 Campobello Road, MlssJssauga, Ontano, L5N 2L8 Tel: (905) 817-5700 Toll-free: 800-563-6266 Fax: (905) t3 "ll<"jl i 7 \',JWV'l.rna:.:xan1 t;a 
Ma?§i.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 

Maxxam /\nalyllcs lmernalional Gorporat1on o/a Maxxam Anal~ltics 6740 Campobello Road, MISSissauga, Ontario. L5N 2L8 Tel: (905} 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 \Y\Vw.maxxam.C<::I 
Ma({)lam 

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 

ICP1/MS 3177251 2013/04/10 

Page4 of8 

f\lla'(,xarn t ... nalylics International Corporation o/a Maxxam Analytics 6740 Campobello Road, Mlssissauga, Ontarlo, L5N 2L8 Tel: (905) 817~5700 Toti~Free: 800-563-6266 Fax: {905) 817-5777 www.ma'(xam.ca 
Ma?§i.am 

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 only to the items tested. 

Page5of8 

1\!lauam Analylics Jrnernational Corporation o/a Maxxam Analytics 6740 campobello Road, Mlsslssauga, Ontario, L5N 21.8 Tel: (905) 817·5700 Toll-Free: 80Q-563·6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma-§.am 

QA/QC 

Batch 

Num lnit QCTvoe 

3177251 N_R 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 

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 vvvv/mrn/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) 2013104/12 

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 (Ni) 2013/04/12 

Value %Recoverv 

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- 130 

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 

'V~::l'xx<-~rn twalvucs lntE'rnational r..orporallon o!a Maxxam Anatytics 67<10 C.arnpobeJio Road, Mlss1ssauga, ontarto,LSN 2L8 Tel: (905) 817 .. 5700 Toii~Free: 80()..563~6266 Fax: (905) 817~':..•777 W\Vw.maxxam.t:.a 
Ma"f}i.a m 

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. 

Page7of8 

Ma-.am AnalyUcs lrtternational COrporation o/a Maxxam Analytics 6740 Campobello Roa~. Mlssissauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma-§.am 

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 5.1 0.2 of 

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

Page8of8 

1\ilaxxam Analytics lmernational COrporation o/a Maxxam Analylics 6740 GampoDello Road, Mlssissauga, Ontario, L5N 2L8 Tel: (905j 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
~ ,--...,.,_.,I.e-?;~ .~· 

_..... LJ. ~.E~ 

Sorbent Trap Analysis Report 

Client Name Keika Ventures, LLC 

Contact Name Lorri White 

Trap 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 

Less than 0.027 ng is considered "< LDL." Which is less than the lowest 

detection limit. 

!Calibration Report Available I 

~Variability ±1 O'VO! 

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 

v-.. .... J.I'.fi .. Jhi'J!umex.·.:'Jn: 

Project Number 2001307 

Turn -Around Time 

0 Standard 

D 48 hour rush 

Other 

Date 4/11/2013 

Phone 919-933-9569 __ ~~~~~~----

Massng Massng Spike BreakSect.2 Sect.3 Level (ng) through% Comments 

0.74 Field Blank 

0.54 20 Train Blank 

0.54 Train Blank 

0.61 #5 Baahouse, Center 

0.52 #5 Baghouse, Center 

0.74 #5 Baghouse, Center 

0.55 #5 Baghouse, Center 

0.74 20 #5 Baghouse, Center 

0.47 #5 Baghouse, Center 

0.72 #2 Baghouse, Center 

0.72 #2 Baghouse, Center 

0.87 #2 Baghouse, Center 

0.72 #2 Baghouse, Center 

0.73 #2 Baghouse, Center 

0.57 20 #2 Baghouse, Center 
Mar:{)2.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. 

Encryption Key~ ;/I Ancy Sebastian 

f/(;1.~P¥d. w- 29 Apr 2013 23:03:49 -04:00 

Please direct all qu O>UVIIO> ICl:JC:UUIII!:I und 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) 

EPA 1613Bmod(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 

!\/laxxam Ana!vlics lmernalional COrporatiOn o.'a Maxxam Analytics 6740 Campobello Road, Mlssissauga, Ontano,l5N a..B Tel: (905) 817~5700 Toll-Free: 80o-563-6266 Fax: (905) 817-5777 W\'YW.max:xam.ca 
Ma(552arn 

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 

COC Number N/A TOXIC EQUIVALENCY 

Units TRAIN EDL RDL 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 0.038 0.30 0.00030 0.000024 

233'44'-PentaCB-( 1 05) 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 ~.031 0.30 0.10 0.0031 

HexaCB-( 156)+(157) ng 0.17 0.033 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 0.030 0.30 0.000030 0.00000090 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.0045 

Surrogate Recovery (%) 

C13-233'44'55'-HeptaCB-(189) % 96 N/A N/A N/A N/A 

C13-233'44'5-HexaCB-(156) % 107 N/A N/A N/A N/A 

C13-233'44'5'-HexaCB-(157) % 107 N/A N/A N/A N/A 

C13-233'44'-PentaCB-(105) % 117 N/A N/A N/A N/A 

C13-23'44'55'-HexaCB-( 167) % 104 N/A N/A N/A N/A 

C13-2344'5-PentaCB-(114) % 114 N/A N/A N/A N/A 

C13-23'44'5-PentaCB-( 118) % 113 N/A N/A N/A N/A 

C13-2'344'5-PentaCB-(123) % 113 N/A N/A N/A N/A 

C 13-33'44'55' -HexaCB-(169) % 97 N/A N/A N/A N/A 

C 13-33'44'5-PentaCB-(126) % 117 N/A N/A N/A N/A 

C13-33'44'-TetraCB-(77) % 119 N/A N/A N/A N/A 

C13-344'5-TetraCB-(81) % 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. 

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 Dioxins and 

Dioxin-like Compounds 

Page2of29 

l\.ila:o:nm t\na!vucs lmernational COrporation o..'a Max.xam Analylics 6740 Campobello Road, Mlssissauga, Ontario,l5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 8"17-5777 www.maxxam.1~ 
Ma?§i.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 

IMaxxam ID RC1497 

!Sampling Date 2013/03/19 

00:01 

COC 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-(1 05) 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 

23'44'55'-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 

C13-233'44'5-HexaCB-(156) % 109 N/A N/A N/A N/A 

C13-233'44'5'-HexaCB-( 157) % 109 N/A N/A N/A N/A 

C13-233'44'-PentaCB-(105) % 114 N/A N/A N/A N/A 

C13-23'44'55'-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 

C13-23'44'5-PentaCB-(118) % 116 N/A N/A N/A N/A 

C 13-2'344'5-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 

C13-33'44'5-PentaCB-(126) % 117 N/A N/A N/A N/A 

C13-33'44'-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, 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 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page3of29 

l\lla'(xam AnalyUcs lmernational COrporatiOn o/a Maxxam Anatytics 6740 campobello Road, Mlssissauga, Ontarto, l5N 2L8 Tel: (905) 817-5700 ToU~Free: 800~563~6266 Fax: (905) 817-5777 \"11\'IIW.max.x.arn.ca 
Ma'62arn 

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 

Sampling Date 2013/03/19 

00:01 

COC 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 0.00000069 

TOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.0065 

Surrogate Recovery (%) 

C 13-233'44'55'-HeptaCB-(189) % 97 N/A N/A N/A N/A 

C13-233'44'5-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) % 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-PentaCB-(114) % 113 N/A N/A N/A N/A 

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 

C13-33'44'55'-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, 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 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page4of29 

Ma<Xam Analylics lrnornational COrporation o!a Maxxam Analytics 6740 Campobello Road, Mlssissauga, Ontario, L5N 2L8 Tel: (905) 817·5700 Toii·Free: 800·563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma?§}.am 

Maxxam Job #: B351227 

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 

Sampling Date 2013/03/19 

00:01 

roc Number N/A TOXIC EQUIVALENCY 

Units RUN EDL RDL TEF (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 0.038 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 0.031 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 (%) 

C13-233'44'55'-HeptaCB-(189) % 94 N/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 

C13-233'44'-PentaCB-(105) % 109 N/A N/A N/A N/A 

C13-23'44'55'-HexaCB-(167) % 100 N/A N/A N/A N/A 

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 

C 13-2'344'5-PentaCB-( 123) % 103 N/A N/A N/A N/A 

C13-33'44'55'-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 

C13-344'5-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 

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 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 5 of29 

\rlaxxam/\nalyucs lrnernalional CorporatiOn o:'a Maxxam Anal~/tics 6740 Campobello Road, MlsS1ssauga, OntariO, LSN 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.t.:a 
Ma?9-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 

IMaxxam ID RC1500 

~ampling 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 p.031 0.30 0.000030 0.00016 

~344'5-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 (%) 

C13-233'44'55'-HeptaCB-( 189) % 94 N/A N/A N/A N/A 

C13-233'44'5-HexaCB-( 156) % 110 N/A N/A N/A N/A 

C13-233'44'5'-HexaCB-(157) % 110 N/A N/A N/A N/A 

C13-233'44'-PentaCB-(105) % 112 N/A N/A N/A N/A 

C13-23'44'55'-HexaCB-( 167) % 107 N/A N/A N/A N/A 

C13-2344'5-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 

C13-33'44'55'-HexaCB-(169) % 111 N/A N/A N/A N/A 

C13-33'44'5-PentaCB-(126) % 123 N/A N/A N/A N/A 

C 13-33'44'-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 

ITEF = 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 

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 (TEQ) value reported is the sum of Toxic Equivalent Quotients for the congeners tested. 

jwH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page6of29 

Ma:o:.am /J,nalyucs lmernallonal COrporation o/a Max.xam Analylics 6740 Campobello Road, Mtssissa-.Jga, OntariO, LSN 2l8 Tel: (905) 8"17-5700 Toll-Free: 800-563-6266 Fax: {905) 817-5717 \V\Vw.maxx.am.t:oo.i 
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 RC1505 

Sampling Date 2013/03/15 

00:01 

COC 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 0.038 0.30 0.00030 0.00014 

233'44'-PentaCB-( 1 05) ng 8.3 0.036 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 O.Q38 0.30 0.000030 0.0000096 

33'44'5-PentaCB-( 126) ng 0.16 0.035 0.30 0.10 0.016 

HexaCB-( 156)+( 157) ng 0.76 0.032 0.60 0.000030 0.000023 

23'44'55'-HexaCB-(167) ng 0.32 0.035 0.30 0.000030 0.0000096 

33'44'55'-HexaCB-(169) ng <0.036 0.036 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 (%) 

C 13-233'44'55'-HeptaCB-(189) % 101 N/A N/A N/A N/A 

C 13-233'44'5-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 

C 13-233'44'-PentaCB-( 1 05) % 121 N/A N/A N/A N/A 

C 13-23'44'55'-HexaCB-( 167) % 120 N/A N/A N/A N/A 

C 13-2344'5-PentaCB-( 114) % 130 N/A N/A N/A N/A 

C 13-23'44'5-PentaCB-( 118) % 129 N/A N/A N/A N/A 

C13-2'344'5-PentaCB-( 123) % 129 N/A N/A N/A N/A 

C13-33'44'55'-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 

~H0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 7 of29 

\·~::·ro.am /•,nalvucs lrrrernauonal Gorporat10n o:a Maxxam Analytics 6"140 CampobeHo Road, MlssiSsauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toii~Free: 800-563~6266 Fa>:: (905) s·H~:)//7 www.rna-.;x.am ~~ 
Mar:{52arn 

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 

Sampling Date 2013/03/15 

00:01 

OC Number N/A TOXIC EQUIVALENCY 

Units RUN EDL ~Dl 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 0.055 0.30 0.00030 0.00013 

233'44'-PentaCB-(105) ng 6.2 0.037 0.30 0.000030 0.00019 

~344'5-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 

~33'44'55'-HeptaCB-( 189) ng <0.030 0.030 0.30 0.000030 0.00000090 

ifOTAL TOXIC EQUIVALENCY ng N/A N/A N/A N/A 0.020 

Surrogate Recovery (%) 

C13-233'44'55'-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 

C13-2'344'5-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 

C 13-33'44'5-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 

C13-344'5-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 

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 

WH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page8of29 

1\i'.axxam Analyucs Jrnernational COrporatiOn o!a Maxxam Analytics 6740 Campobello Road, Mlss1ssauga, Ontaflo, L5N 2L8 Tel: (905) 817·5700 Toll-Free: SO!l-563·6266 Fax: (905) 817·5777 www.maxxam.ca 
Ma§am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

MaxxamiD 

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) 

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 Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 9 of29 

!Viauam Analyllcs l.nernational corporation o:a Maxxam Analytics 8740 CarnpoDeHo Road, MlssJSsauga, omar1o, L5N 2L8 Tel: (905) 817·5700 Toll-Free: 800..563·6266 Fax: {905) 817-5777 www.maxxam.ca 
Mar§l.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) 

RC1495 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units TRAIN EDL RDL TEF (2005 WHO) ~EQ(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 

C13-0ctachlorodibenzo-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 = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro 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 

\•1a~x!irn Ana!ytJcs lrnernalional 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.1~ 
Ma?:{)2am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

MaxxamiD 

Sampling Date 

roc 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 rrEF (2005 WHO) fEQ(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, 

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 

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 

M::~·n..,m/-\naJvucs International COrporation o/a Max.xam Analytics 67-10 Campobello Road, Mlssissauga, Ontarto, L5N 2l8 Tel: (905) 817-5700 Toii~Free: 800-563-6266 Fax: (905) 817-5777 www.maxxarru..a 
Maf§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) 

RC1497 

2013/03/19 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) ~EQ(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 

C 13-12378 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, 

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. 

jwH0(2005): The 2005 World Health Organization, Human and Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

Page 12 of 29 

:Vla:~X::tfll/\nalvllcs International COrporation o/a Maxxam AnalyliCS 6740 Campobello Road, Mlssissauga, Ontano, l5N 2l8 Tel: (905) 817-5700 Toll-Free: 80Q-563-6266 Fax: (905) 817-5777 \~lww.maxxam.ca 
Ma?.S)2.am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

~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) 

RC1498 

2013103119 

00:01 

NIA TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) ~EQ(DL) somers 

2-BH2-M231PCB 

2,3,7,8-Tetra COD* pg <3.7 3.7 30 1.00 3.70 NIA 

1 ,2,3, 7 ,8-Penta COD pg <3.6 3.6 30 1.00 3.60 NIA 

1,2,3,4,7,8-Hexa COD pg <3.6 3.6 30 0.100 0.360 NIA 

1,2,3,6,7,8-Hexa COD pg <3.4 3.4 30 0.100 0.340 NIA 

1,2,3,7,8,9-Hexa COD pg <3.5 3.5 30 0.100 0.350 NIA 

1,2,3,4,6,7,8-Hepta COD pg <3.5 3.5 30 0.0100 0.0350 NIA 

1 ,2,3,4,6, 7,8,9-0cta COD pg 12.3 4.1 300 0.000300 0.00369 NIA 

Total Tetra COD pg 16.1 3.7 30 NIA NIA NIA 

Total Penta COD pg <4.0 (1) 4.0 30 NIA NIA NIA 

Total Hexa COD pg <9.6 (1) 9.6 30 NIA NIA NIA 

Total Hepta COD pg <3.5 3.5 30 NIA NIA NIA 

2,3,7,8-Tetra CDF ** pg <53 (.2) 53 30 0.100 5.30 NIA 

1,2,3,7,8-Penta CDF pg 5.9 3.5 30 0.0300 0.177 NIA 

2,3,4,7,8-Penta CDF pg 6.0 3.3 30 0.300 1.80 NIA 

1,2,3,4,7,8-Hexa CDF pg 8.0 3.4 30 0.100 0.800 NIA 

1,2,3,6,7,8-Hexa CDF pg <3.2 3.2 30 0.100 0.320 NIA 

2,3,4,6,7,8-Hexa CDF pg <4.1 4.1 30 0.100 0.410 NIA 

1,2,3,7,8,9-Hexa CDF pg <4.5 4.5 30 0.100 0.450 NIA 

1 ,2,3,4,6, 7 ,8-Hepta CDF pg 5.9@) 2.3 30 0.0100 0.0590 NIA 

1 ,2,3,4, 7 ,8,9-Hepta CDF pg <3.1 3.1 30 0.0100 0.0310 NIA 

1,2,3,4,6,7,8,9-0cta CDF pg <5.3 5.3 300 0.000300 0.00159 NIA 

Total Tetra CDF pg 335 4.5 30 NIA NIA NIA 

Total Penta CDF pg 67.8 3.4 30 NIA NIA NIA 

NIA = 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 

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 ) EMPC I NOR - Peak detected does not meet ratio criteria and has resulted in an elevated detection limit. 

( 2) RT > 3 seconds - PCDDIDF 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 

'·•la:·c,;.;:.,rn t\nc-~lvucs JmE:'rnatronal Gorpora11on o/a Maxxam Anaty-rics 6740 Campobello Road, MISSJSsauga, Ontarto, LSN 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 \Vww.maxxam.t.:a 
Ma"§.am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

MaxxamiD 

~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) 

RC1498 I 

2013/03/19 

00:01 l 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) fEQ(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 % 76 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDD * % 119 N/A N/A N/A N/A N/A 

C13-1234678 HeptaCDF % 111 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 % 107 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 % 73 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 % 88 N/A N/A N/A N/A N/A 

C13-12378 PentaCDF % 93 N/A N/A N/A N/A N/A 

C13-123789 HexaCDF % 75 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 % 65 N/A N/A N/A N/A N/A 

C13-2378 TetraCDF % 85 N/A N/A N/A N/A N/A 

C13-0ctachlorodibenzo-p-Dioxin % 105 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 

* CDD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEQ = Toxic Equivalency Quotient, 

pc 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 Mammalian Toxic Equivalency Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 14of29 

Ma.<xam Analyllcs Jrnernalional COrporation o!a Maxxam Anal~"tics 6740 Campobello Roa~. Mlssissauga. Onlarlo. LSN 21..8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) !117-5117 www.m11uam.t.a 
Ma"§am 

Maxxam Job #: 6351227 

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) ~EQ(DL) somers 

3-BH2-M23/PCB 

2,3,7,8-Tetra COD* pg <4.1 4.1 30 1.00 4.10 N/A 

1 ,2,3, 7 ,8-Penta COD pg <4.1 4.1 30 1.00 4.10 N/A 

1,2,3,4,7,8-Hexa COD pg <3.9 3.9 30 0.100 0.390 N/A 

1,2,3,6,7,8-Hexa COD pg <3.8 3.8 30 0.100 0.380 N/A 

1 ,2,3,7,8,9-Hexa COD pg <3.8 3.8 30 0.100 0.380 N/A 

1 ,2,3,4,6, 7 ,8-Hepta COD pg <3.2 3.2 30 0.0100 0.0320 N/A 

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 N/A N/A N/A 

Total Penta COD pg 4.9 4.1 30 N/A N/A N/A 

Total Hexa COD pg <9.8 (1) 9.8 30 N/A N/A N/A 

Total Hepta COD pg <3.2 3.2 30 N/A NIA NIA 

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 NIA 

1 ,2,3,4, 7 ,8-Hexa CDF pg <13 (3) 13 30 0.100 1.30 NIA 

1,2,3,6,7,8-Hexa CDF pg <5.2 (3) 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 NIA 

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 NIA 

1,2,3,4,7,8,9-Hepta CDF pg <4.0 4.0 30 0.0100 0.0400 NIA 

1,2,3,4,6,7,8,9-0cta CDF pg 5.3 3.6 300 0.000300 0.00159 NIA 

Total Tetra CDF pg 455 2.9 30 NIA N/A NIA 

NIA =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 

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 interference 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 

:>;Ja.xam Analyucs lmernational COrporatiOn o!a Maxxam Analytics 6740 CampoDello Road. MlssiSsauga. Ontario. L5N 2L8 Tel: (905) 817-5700 Toll-Free: BOQ-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma?:{)2am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

MaxxamiD 

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) 

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 

ifOTAL 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 = Chloro Dibenzo-p-Dioxin, •• CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEQ = 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 

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 

Page 16 of29 

v.,·.x•m Anal'/l!GS lmernallollal <.orporatlon o!a Mal<Xam 1\nalyliCS 6740 C<Jrnpobello Road, Mlsslssauga, OntarJO,l5N 21.8 Tel: (905) 8.17·5700 Tofl·free: 80()..563·6266 Fax: (905) 817·5777 V.!Ww.maxxam ca 
Ma?.S}2am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

MaxxamiD 

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) 

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 

Total 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 

~otal 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 

* CDD = 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 Factors for Dioxins and 

Dioxin-like Compounds 

( 1 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

Page 17 of 29 

Maxx"m AnalyLJcs Jmernational COrporation o1a Maxxarn Analylics 6140 Canpobello Road, Mlssissauga, Ontario, L5N 21..8 Tel: (905) 817-5700 Toll-free: soo-563-6266 fax: (905) 817-5777 www.maxxarn.ca 
Mar{)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) 

RC1500 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) TEQ(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 = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro Dibenzo-p-Furan 

TEF = Toxic Equivalency Factor, TEO = Toxic Equivalency Quotient, 

pc 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 of29 

\·~;.J_x xi'lrn /\nalyl!cs lnternalional Corporcnron o/a Max.xam Analy·iics 6740 Campobello Road, MlSsrssa~Jga, Onlano, L5l\l 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 8 ·n-5777 www.maxxanu . .:a 
Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam 10 

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) 

RC1505 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) TEQ(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 N/A 

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 N/A 

1 ,2,3,6,7,8-Hexa CDF pg 11.3 (1) 3.4 30 0.100 1.13 N/A 

2,3,4,6,7,8-Hexa CDF pg 8.4 4.3 30 0.100 0.840 N/A 

1 ,2,3, 7 ,8,9-Hexa CDF pg <4.8 4.8 30 0.100 0.480 N/A 

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 

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, 

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 

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 exceeds expected retention time (from internal standard) by 

greater than 3 seconds. 

( 3 ) EMPC I Merged Peak 

Page 19 of29 

\·~~;_-.:..;~r1l/•,nc:~~vtJ;_;s !mernat1oncll Corpora11on o/a Maxxam Analyt!CS 57<10 Campobello Road, Mlss1ssauga, Ontano, L5N 2L8 Tel· (905) 817-5700 Toll-Free· 800-563-6266 Fax: (905) 81l<J17? \VWw.m;:txxcuni..a 
Ma(!52am 

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) 

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 

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 

C13-0ctachlorodibenzo-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 

• CDD = Chloro Dibenzo-p-Dioxin, ** CDF = Chloro 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 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 

Mauam AnaiVl!CS lmernational COrporatiOn o!a Maxxam Anal~'lics 6740 campobello Road, MISSISsauga. 001ar1o, L5N 2L8 Tel: (905) 817-5700 Toll-Free: aoo-563-6266 Fax: (905) 817-5777 wwwmaxxam.ca 
Ma?!.}2am 

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) 

RC1511 

2013/03/15 

00:01 

N/A TOXIC EQUIVALENCY #of 

Units RUN EDL RDL TEF (2005 WHO) fEQ(DL) somers 

3-BH5-M23/PCB 

2,3,7,8-Tetra CDD * pg 9.5 (1) 3.5 30 1.00 9.50 N/A 

1,2,3,7,8-Penta CDD pg 6.6 3.4 30 1.00 6.60 N/A 

1 ,2,3,4,7,8-Hexa CDD pg <3.3 3.3 30 0.100 0.330 N/A 

1 ,2,3,6,7,8-Hexa CDD pg <3.2 3.2 30 0.100 0.320 N/A 

1 ,2,3,7 ,8,9-Hexa CDD pg 4.6 3.2 30 0.100 0.460 N/A 

1 ,2,3,4,6, 7 ,8-Hepta CDD pg 5.9 (1) 3.1 30 0.0100 0.0590 N/A 

1 ,2,3,4,6, 7 ,8,9-0cta CDD pg 26.5 (1) 4.7 300 0.000300 0.00795 N/A 

Total Tetra CDD pg 326 3.5 30 N/A N/A N/A 

Total Penta CDD pg 105 3.4 30 N/A N/A N/A 

Total Hexa CDD pg 4.6 3.3 30 N/A N/A N/A 

Total Hepta CDD pg 5.9 (1) 3.1 30 N/A N/A N/A 

2,3,7,8-Tetra CDF ** pg <460 (2) 460 30 0.100 46.0 N/A 

1 ,2,3, 7 ,8-Penta CDF pg 46.3 3.8 30 0.0300 1.39 N/A 

2,3,4,7,8-Penta CDF pg 38.1 3.6 30 0.300 11.4 N/A 

1 ,2,3,4,7,8-Hexa CDF pg 26.8 2.5 30 0.100 2.68 N/A 

1 ,2,3,6,7,8-Hexa CDF pg 13.4 2.3 30 0.100 1.34 N/A 

2,3,4,6,7,8-Hexa CDF pg 5.1 3.0 30 0.100 0.510 N/A 

1 ,2,3,7,8,9-Hexa CDF pg <3.3 3.3 30 0.100 0.330 N/A 

1 ,2,3,4,6, 7 ,8-Hepta CDF pg 10.1 (1) 3.7 30 0.0100 0.101 N/A 

1 ,2,3,4,7,8,9-Hepta CDF pg <5.0 5.0 30 0.0100 0.0500 N/A 

1 ,2,3,4,6, 7 ,8,9-0cta CDF pg 33.6 5.2 300 0.000300 0.0101 N/A 

Total Tetra CDF pg 3230 4.0 30 N/A N/A N/A 

Total Penta CDF pg 757 3.7 30 N/A N/A N/A 

Total Hexa CDF pg 118 2.7 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, TEO= 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 ) EMPC I Ratio - Isotopic ratio adjusted to meet theoretical 

( 2 ) RT > 3 seconds - PCDD/DF analysis - Peak detected exceeds expected retention time (from internal standard) by 

greater than 3 seconds. 

Page 21 of29 

Ma.xxi.-lrn /\n<11VlJCS lmernational Corporauon o/a Maxxam Ana!ytics 6740 Campobello Road, Mlsstssauga, Ontario, L5N 2l8 Tel: (905) 817-5700 Toll-Free: 300-563-6266 Fax: (905) 817-5777 \'11\Vw.maxxam.t..a 
Ma~am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID 

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) 

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 N/A 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 

C 13-0ctachlorodibenzo-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 = Chiaro Dibenzo-p-Dioxin, ** CDF = Chiaro 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 

Page22 of29 

l\fl.a'<xam t ... nalvucs lrnernational Corporation o:a Maxxam Anal~"tics 6740 Campobello Road, Mlssissat.Jga, Ontario, L5N 2LB Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 \'V\'IJW.maxxam.t:;a 
Ma?§).am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Test 

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 

D escr1pt1on 

2 3 7 8-TCDF Confirmation (M23) 

Dioxins/Furans in Air (Method 23) 

PCB Conoeners in Air (1668A) 

Maxxam ID RC1498 

Sample ID RUN 2-BH2-M23/PCB 

Matrix Stack Sampling Train 

T D est escnpt1on 

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 

12 3 7 8-TCDF Confirmation CM23) 

IDioxins/Furans in Air (Method 23) 

IPCB Conoeners in Air (1668A) 

Maxxam ID RC1500 

Sample ID RUN 1-BH5-M23/PCB 

Matrix Stack Sampling Train 

T es tD escnpuon 't' 

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 

nstrumentatlon B h ate E xtracte d 

HRMS/MS 3191218 N/A 

HRMS/MS 3190066 2013/04/16 

HRMS/MSEC 3182506 2013/04/16 

I ns tr umen tati on B ac t h Ext ra cted 

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 

I ns t rumen tat' IOn B ac t h E t x ra ct e d 

HRMS/MS 3191218 N/A 

HRMS/MS 3190066 2013/04/16 

HRMS/MSEC 3182506 2013/04/16 

Page23of29 

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 

Analyzed 

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 

A na1yst I 

Vica Cioranic 

Owen Cosby 

CathvXu 

Collected 2013/03/19 

Shipped 

Received 2013/04/06 

A na1ys I t 

Vica Cioranic 

OwenCosbv 

Cathy Xu 

Collected 2013/03/19 

Shipped 

Received 2013/04/06 

Analyst 

Vica Cioranic 

Owen Cosby 

CathvXu 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

A na1ys I t 

Vica Cioranic 

OwenCosbv 

Cathy Xu 

Ma<>am Analylics lmernational COrporation o!a MaJU<am Anal~'lics 6740 GampobeDo Road, MISSISsauga, OntariO, L5N 21.8 Tel: (905) 817-5700 Toll-Free: 80Q-563-6266 Fax: (905) 817-f>777 www.maxxam.ca 
Ma?Y2am 

Maxxam Job #: 8351227 

Report Date: 2013/04/29 

Maxxam ID RC1505 

Sample ID RUN 2-BH5-M23/PCB 

Matrix Stack Sampling Train 

T D est escr1pt I i on 

2 3 7 8-TCDF Confirmation (M23) 

Dioxins/Furans in Air (Method 23) 

PCB Congeners 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) 

I Dioxins/Furans in Air (Method 23) 

I PCB Conaeners in Air C1668A) 

Keika Ventures 

Client Project#: Tl1550 

Site Location: TEST INC. - FELMAN PRODUCTIONS 

Your P.O. #: 10244 

Test Summary 

nstrumentat on 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 

Page24 of29 

A na1yze I d 

2013/04/24 

2013/04/25 

2013/04/24 

Analvzed 

2013/04/24 

2013/04/25 

2013/04/24 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

A nalyst 

Vica Cioranic 

Owen Cosby 

Cathy Xu 

Collected 2013/03/15 

Shipped 

Received 2013/04/06 

Analvst 

Vica Cioranic 

Owen Cosby_ 

CathvXu 

Manam AnaiV!IGs lrnernatlonal Corporation ola l\llaxxam Analy!lcs 6740 C<~rnpoDello Road,l\lllll!!ll!sauga, Ontario, L5N 21.6 Tel: (1105) 817·5700 Toii·Free: 80()-563·6266 Fax: (905) 817·5777 www.ma><"am.r.a 
M af.S52a rn 

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 

Page 25 of29 

'\ii:·n; x~~n /o~,na!vllc-:: lmernational Gorpor<11.1on o:a Max:~~; am Analylics 0740 Campobello Road, MlssJssauga, 0n1ar1o, L5N 2L8 Tel: (905' 817~5700 Toll-Free: 800-563-6266 Fax: {905) a·17-G777 \".1\Vw.maxx.am.i.:a 
Ma[{)2am 

QA/QC 

Batch 

Num lnit QCType 

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 vvvv/mm/dd 

C13-233'44'55'-HeptaCB-(189) 2013/04/24 

C13-233'44'5-HexaCB-(156) 2013/04/24 

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 

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-(1 05) 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) 2013/04/24 

233'44'55'-HeptaCB-(189) 2013/04/24 

C13-233'44'55'-HeptaCB-(189) 2013/04/24 

C13-233'44'5-HexaCB-(156) 2013/04/24 

C13-233'44'5'-HexaCB-(157) 2013/04/24 

C13-233'44'-PentaCB-(105) 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 

Page26of29 

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 

Mauam Analytics Jrnernational COrporation ola Maxxam Analytics 6740 GampobeHo Roa~. MlssiSsauga, Ontano, L5111 2LB Tel: (905) 817-5700 Toll-Free: aoo-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma?§J.am 

QNQC 

Batch 

Num lnit QCType 

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 yyyy/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 COD 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 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 

1,2,3,4,6, 7 ,8-Hepta CDF 2013/04/25 

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

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 

Page27of29 

Value %Recovery 

<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 

Ma'Xam Analylics Jrnernational Corporation o!a Maxxam Analytics 6740 Campobello Road. Mlss1ssauga. Ontario. L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma?§}.am 

QNQC 

Batch 

Num lnit QCType 

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 

C13-0ctachlorodibenzo-p-Dioxin 2013/04/25 

2,3,7,8-Tetra CDD 2013/04/25 

1,2,3,7,8-Penta CDD 2013/04/25 

1,2,3,4,7,8-Hexa CDD 2013/04/25 

1,2,3,6,7,8-Hexa CDD 2013/04/25 

1,2,3,7,8,9-Hexa CDD 2013/04/25 

1 ,2,3,4,6, 7 ,8-Hepta CDD 2013/04/25 

1 ,2,3,4,6, 7,8,9-0cta CDD 2013/04/25 

Total Tetra CDD 2013/04/25 

Total Penta CDD 2013/04/25 

Total Hexa CDD 2013/04/25 

Total Hepta CDD 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 %Recovery 

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. 

Page28of29 

Mauam AnalyUos International COrporation o/a Maxxam Analylics 6740 campobello Road. Mlssissauga. Ontario. L5N 2L8 Tel: (905) 817-5700 Toll-Free: 80D-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma?SJ.am 

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 

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 29 of29 

Ma.xxam AnalvUcs International CorporatJon o!a Max.xam Analytics 5740 Campobello Road, Mlsslssauga, Ontario, L5N 2L8 Tel: {905) 817-5700 Toll-Free: 800~563-6266 Fax: (905) 817-5777 Vif\'YW.maxxam.ca 
Ma"§.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: 2013/05/02 

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 KeyE ;/I 1 kocy Sebastian 

v~~- 02 May 201316:52:06-04:00 

Please direct all qu :suum• ""!::l~tunty um: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 

CARB 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 

1\ilaxxam Analytics lmernational Corporation ola Maxxam Analytics 6740 campobeno Roao. Mlssissauga, Ontario. L5N 21.8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817·5717 www.m1"'xam.oo 
Ma62-am 

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 

~ampling 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 :;oL 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) 

Pyrena 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 ~.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-2H1 0 o/o 66 NtA N/A 55 N/A N/A 43 (2) 

Acenaphthylene-2H8 o/o 64 NtA N/A 78 N/A N/A 67 

Anthracene-2H1 0 o/o 42 (2) NtA N/A 95 N/A N/A 72 

Benz(a)anthracene-2H 12 o/o 98 ~/A N/A 74 N/A N/A 142 

Benzo(a)pyrene-2H12 o/o 48 (2) N/A N/A 93 N/A N/A 90 

Benzo(b )fluoranthene-2H12 o/o 76 N/A N/A 109 N/A N/A 91 

Benzo(g,h,i)perylene-2H12 o/o 54 N/A 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 

FDL RDL ~c 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 

!V;,.xxem Analyucs lrnernalional Corporation ora Maxxam Analytics 6740 Campobello Road. Mlssissauga. omar•o. L5N 21.8 Tel: (905) 817-5700 Toll-Free: 800..563-6266 Fax: (905) 817-5777 www.maxxam.r..a 
Ma?§l.am 

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 

~ampling 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 i;DL RDL RUN 1-BH2·PAH EDL RDL RUN 2·BH2·PAH 

BLANK·PAH 

Benzo(k)fluoranthene-2H12 % 75 1'-JIA N/A 98 N/A N/A 65 

Chrysene-2H12 % 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-2H 1 0 % 79 NtA N/A 88 N/A N/A 88 

Fluorene-2H1 0 % 123 NtA N/A 70 N/A N/A 68 

lndeno(1,2,3-c,d)pyrene-2H12 % 51 NtA N/A 98 N/A N/A 103 

Naphthalene-2H8 % 71 NtA N/A 46 (1) N/A N/A 35 (1) 

Perylene-2H 12 % 54 ~/A N/A 83 N/A N/A 75 

Phenanthrene-2H1 0 % 44 (1) NtA 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 Umit 

EDL = Estimated Detection Umit 

QC Batch = Quality Control Batch 

FDL RDL ~c 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 

Ma.xxem Ana!yllcs lrnerna1ional C',orporation o/a Maxxam Analyllcs 6740 Campobello Road, Mlssissauga, Ontario, L5N 2LB Tel: (905) 817·5700 Toii·Free: 800·563·6266 Fax: {905) 817·5777 www.maxxam.r.:a 
Ma?:52am 

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 

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) 

Pyrena 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-2H 1 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-2H 12 % 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 

1\'~::~'o:.am Ana!vucs 1mernat1ona1 Corporation ota Maxxam Analytics 6740 CarnpoiJeiJo Roac1, Mlsslssauga, Ontarlo,LSN 2L8 Tel: (905) 817 .. 5700 Toii~Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma"62am 

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 

MaxxamiD 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 

Benzo(k)fluoranthene-2H 12 % 101 N/A 86 N/A N/A 88 

Chrysene-2H12 % 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-2H1 0 % 88 N/A 99 N/A N/A 99 

Fluorene-2H1 0 % 66 N/A 70 N/A N/A 72 

lndeno(1,2,3-c,d)pyrene-2H12 % 114 N/A 110 N/A N/A 105 

Naphthalene-2H8 % 34 (1) N/A 33 (1) N/A N/A 42 (1) 

Perylene-2H12 % 80 N/A 61 N/A N/A 57 

Phenanthrene-2H1 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 

EDL 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 

'\11~: ... x2ln1 Ana!Vtlcs JrnE'mational C..orporation o/a Maxxam AnaJyUcs 6740 CampobeJio Road, Mtss1ssauga, Ontarlo,l5N 2l8 Tel: (905) 817-5700 Toti~Free: 800~563~6266 Fax: (905) 817~5777 v.tww.maxxam.f..a 
Maf§2am 

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 

lrQC Number N/A 

Units RUN 3-BH5-PAH EDL RDL be Batch 

Naphthalene ng 31100 (1) 330 500 3182508 

2-Methylnaphthalene ng 19100 130 500 3182508 

2-Chloronaphthalene ng 52.5 0.27 10 3182508 

~cenaphthylene ng 3760 51 500 3182508 

Acenaphthene ng 2370 270 500 3182508 

Fluorene ng 2280 200 500 3182508 

Phenanthrene ng 36900 (1) 120 500 3182508 

~nthracene ng 1360 140 500 3182508 

Fluoranthene ng 18200 130 500 3182508 

Pyrena 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-2H 1 0 'Yo 42 (2) N/A N/A 3182508 

Acenaphthylene-2H8 'Yo 61 N/A N/A 3182508 

Anthracene-2H 1 0 'Yo 51 N/A N/A 3182508 

Benz(a)anthracene-2H 12 'Yo 174 {2) N/A N/A 3182508 

Benzo(a)pyrene-2H12 'Yo 54 N/A N/A 3182508 

Benzo(b )fluoranthene-2H12 'Yo 128 N/A N/A 3182508 

Benzo(g,h,i)perylene-2H12 'Yo 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 

\·1:-!xx~rn/},lln~vucs lnwrnalional Gorpora:tJon o:a Maxxam Anaty·ucs 6740 Campobello Road, Mtssissauga, Ontario, L5N 2LB Tel: (905) 817-5700 Toti-Free: 800-563-6266 Fax: (905) 817-5777 \"·tww.maxxam.r.,;a 
Ma'652am 

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 

roc Number N/A 

Units RUN 3-BH5-PAH EDL RDL QC Batch 

Benzo(k)fluoranthene-2H12 % 94 N/A N/A 3182508 

Chrysene-2H 12 % 112 N/A N/A 3182508 

Dibenzo(a,h)anthracene-2H14 % 132 N/A N/A 3182508 

Fluoranthene-2H1 0 % 88 N/A N/A 3182508 

Fluorene-2H1 0 % 79 N/A N/A 3182508 

lndeno(1 ,2,3-c,d)pyrene-2H12 % 112 N/A N/A 3182508 

Naphthalene-2H8 % 35 (1) N/A N/A 3182508 

Perylene-2H 12 % 56 N/A N/A 3182508 

Phenanthrene-2H1 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 

Maxxam /;nalvtms lmernational COrporatJon o!a Maxxam Anal~"tics 6740 Campobello Road, Mlssissa!J!Ja. Ontario, LSN 2LB Tel: (905j 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-5777 www.maxxam.ca 
Ma('{)2.arn 

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 

HRMS/MS 3182508 2013/04/16 

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 

HRMS/MS 3182508 2013/04/16 

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 Anal zed Anal st 

HRMS/MS 3182508 2013/04/16 2013/05/01 Edmond Mcneil 

Page 8 of 12 

f\r1axx<c~rn /~n?.IVHGS lrnernalional Gorporalion o/a Maxxam j!."\naly-lics 6740 Campobello Road, MISSISSauga, Ontario,l51\12l8 Tel: (905) 817~5700 Toll-Free: 800-563-6266 Fax: (905) 8-17-5177 WWWJ'mt.'<X<:llll.t.a 
Ma({)2arn 

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 only to the items tested. 

Page 9 of 12 

1\ila.xxam Analylics tmernational COrJJOration ora Max.xarn Analytlcs 6740 Camj)Obeno Road, MlsSISsauga, On!ario, L5N 21.8 Tel: (905) 817-5700 Toll-Free: 80Q-563-6266 Fax: (905) 817-5777 wwwmaxxam.ca 
Ma?§i.am 

QA/QC 

Batch 

Num lnit QCType 

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-2H12 2013/04/30 

Benzo(a)pyrene-2H12 2013/04/30 

Benzo(b )fluoranthene-2H12 2013/04/30 

Benzo(g,h,i)perylene-2H12 2013/04/30 

Benzo(k)fluoranthene-2H 12 2013/04/30 

Chrysene-2H12 2013/04/30 

Dibenzo(a,h)anthracene-2H14 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 1 0 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 

\·13'o..:am/-\na!vllcs Jmernational COrporation o/a Maxxam Anatytics 6740 campobello Road, MISSissauga, Ontario, L5N 2L8 Tel: (905) 817-5700 Toll-Free: 800-563-6266 Fax: (905) 817-~717 www.maxxarn.1~ 
Ma?§l.am 

QAIQC 

Batch 

Num lnit QCTvoe 

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-2H12 2013/04/30 

Benzo(a)pyrene-2H12 2013/04/30 

Benzo(b )fluoranthene-2H12 2013/04/30 

Benzo(g,h,i)perylene-2H12 2013/04/30 

Benzo(k)fluoranthene-2H 12 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-2H 12 2013/04/30 

Phenanthrene-2H1 0 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 2013/04/30 

Benzo(e )pyrene 2013/04/30 

Benzo(a)pyrene 2013/04/30 

Perylene 2013/04/30 

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 %Recoverv 

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=0.70 

<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 

% 50 

% 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 

no 

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 

Me.u""' Analytic> lrrternauonal C',orporauon o:a Mal<.Xam Analytics 6740 Campobello Road. MISSISSauga. Ontario. LSN 21.8 Tel: (905) 817·5700 Toll·free: 80()-563·6266 Fax: {905) 817·5777 www.maxxam.ca 
Ma?§i.am 

Validation Signature Page 

Maxxam Job #: 8351259 

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

Owen Cosby, BSc.C. hem, Supervisor, HRMS Services 

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(£), signing the reports. For Service Group specific validation please refer to the Validation Signature Page. 

Page 12 of 12 

Manam Analvlics Jrnernatlonal Gorporauon o/a Maxxam AnalytJcs 87411 Campobello Road, Mlss!Ssauga, Ontar10,L5lll 2l6 Tel: (905) 817·5700 Toii·Free: aoo-563·6266 Fax: (905) 817·5777 www.maxxam.ca 
APPENDIXD 

FIELD DATA SHEETS . -~ 
Comments: :3 c ~.fG; c L.j ( 

.. ~ 7 1 S""l fo s-f _ __:_...:__;;;_,_........,._-,--- Sampling Data .l £)". 3 JS'@ G. 5 ProJ.~ct,~r"~j;;'$~~ O Meter ?ox #,_;;l_O_io-. -'-, ... -C"lf-.-"':..-, =-><c;._;:..:..::...Yo.;:_G_0.....:2~-e-.-,-1--I-m_p..:... '---,-,--------l 

. · Plant f-.,~{Mt:vl MeterCal.(Y) t~030Z'" %9i>:b>V/;i' 1 

Unit/Stack ~,:·5 .B H .. Pitot Cal. (Cp) o ·~!.f . %co· ··1·'~'·, 2 

Operator /3 fL Nozzle # %N2 3 --- Run# 1 '· sff).,. .., Nozzle [)ia. (in.) t, f A~sumed Moist% 4 

Date 3} f 5' {JJ · ' ,.. . . StackDia;(i~.) ' .. ,< .' • Final Moist,~====== 5 

Snmple Time_fbQ __ , ___ Stati~,Press,("Hg.) (), ( 0 Final Isokinetic %.: 6 

. -~"'· Min!pt - . · P,ress. ''Hg) _E~ :o1) Initial Leik Rate....,~-----

, Filt«r # ' . · f Final Leak·R~te 

···, 

I 

' 

,~ 

·~ ·: -- -. 

j 

·I 

i 
' 

I 

TEST, Inc. 

_....J...H~L_· .L-J _"':"""'?"""....,..........- Sampling Data 

ProJect# If[() Meter Box# )010 %C02'-0~ .. ~~P· Initial 

Plant F t ( ~ev\.. 5 \. Meter Cal (Y) W03 ·. %02 ;Jo. :f 1 -

Unit/Stack .. -*) /JH ')i .. ~'Pitot Cai.(Cp),_'·__ %CO~~--"-

Operator ---:::-·..b~='Z.::,_____ ~?zzle # ___ , %N2 --·~.._· ,_-

2 

3 

Run# ).. . ,'Nozzle Dia. {in.) Assumed Mois~% ' ·,. 4. 

-Date _ ____,_~-T~~ '_ Stack Dia.(in.),•~f'. f Final Moist.% . 5} 

Sample Time 1 ).(U · _ Static Press.('.'Hg:.) __ ·.;_ Final Isokin~~ic %________ · 6'~~ __________ j _____ . 

Min!pt f .... . . Bar. Pi'ess. ("Hg) 1.-"J,O..'J !nitial Leak Rate __t2_Q N cfir1,@ /0 . ''Hg 

Filter# \Leak Check V, 1. · Final.Leak Rate , 6o fm @ __,_ 0 · 

Port/ 

. Point 

.3 

V acuu · Stack 

! 

!-.~~~~~~~~~~ " 

·,, 

\ ...•. : 

,_L •••• __________ :"!., ____ • ••• ··--

I 

I 

I 

1 

1 

i 

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! 
:~ . 

TEST, Inc. 

frtCI 

Comments: r 

3«6 . .3ts e ~ J 

SamplingData ~9~o,t5f 5" ----~~--~ ~----------~~----------------~ 

Proje~t # t 5" f () Meter Box# J.O I 0 %C02 (). '-/ 

Plant F-~ ( """"""" Meter Cal. (Y) I· a:?o.3 %02 dO· y 

Unit/Stack ~ 5'" /J H Pitot Cal. '(Cp) • (pf %CO . 

Operator •Dj:. Nozzle # %N2 

Run# ~ · .· Nozzle Dia. (in.)_(_,?..,...-- Assumed Moist%_· __ 

Final Moist. % 

Imp:-

1 

2 

3 

4 

Date ) /1'5' It] Stack Dia.(in.)_____,_ 5 

Sample Time L 1..0 Static Press.("Hg.) 1-0 Final Jsokinetic% _ -··---·-··· f> 

Min/pt ; Bar. Press. ("Hg)Q?E;c;s- Initial Leak Rate D cfrn@ 10 'Hg 

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

Dry Gas Pitot v~ 1i o.~ .. ~tl( Vacuu Stack Probe Filter Imp. . .. ! Dr) Gas 

Pqrt/ Tirpe Meter (CF) Velocity ~w m Temp .. . Temp. Temp . Temp. Temp. 

Point 7'J'""S"" .. 7<l5.f.uDJ ("H20) 

II 

( (cfm) ("Hg.). (F) (F) (F) (F) In Out 

,:) 7J lJJtJ() 71'1&0~ <:) ,(:()C. "i 1)'0 /. 8 5o /;;ll ·;;sY ps-f (a) rei {pf( 

7. 8"!6) &:;3/ltJ;l C>._ooo~ 7tv l·8 5'.D /:J.t; -~y_:r- ?50 &1 ~ &1 

/p ZJtO <j()7.,Jo£ 5.DDOLf .. 75Jo /.'? ~<":0 J;J-0 ?47 !;;{'-Pi> &3 ILP:r (ti(J 

s- 85JS"r Y Jl tl.DIP tr oo-o'-1 ,-:Jfi'CJ 1.71 .S:CJ IJ.I j)j ;;so ~ 70 ~8' 

4 8'J..O 'iLJ" J a?/ IJ.tJaYf ,/'XO ;.r '{;() !J/ b;ls-J ~ 5<L 10 (tfl 

3 ({J-5' '119/0·(R IJ,iJtZJ<./ 7_ 'irl) l?f 5lJ 1;)0 ~s-D· d4Cf 53 tit fo7 

d 83o 1i;;l_ ~ .0 {) 7 {).{)ODI.j J'ifl) J.ff s:o ld-1 ~- OJ-5::) .n t.Pz tas 

I ff3o >f~b.?IJ7 /'). tJa::N 7.3D J. 5l ,1:'/) .. i '2 I ,;2:>3• .;2'-!1 51e /_py &7 

'giL/f) ~..2&!.9b7 .· 

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l~3Lfloo.~'+ .-~ •• ·~ ·- -· < 

,. g-)JZ) 7116 {,,? s: C) ' / lf /-:: __ ~ .. :J 57 " ;257)__ ){.'; 

~-~1 '""·-···· ... -··--' 

~~· .--8'"15J r:J?t~o I:J o.&n 'I h~ lr?' 5"""LJ rt'-I~D ;l·JC) e?-.53 s=t. 

s- 9t.OO 141/ 0,1' CJ.()OOY 7~(;· /,] s.o I <-17 ;;iJ"ij ;;2.50 ~ . &7 L6l 

l.f ; ?! cxir/lla..OOtl-~ (},(Xt)l.f' i 714& : , .. 7 i -~() i/'14 : ;.s-; :;; 50 , 5?:t i tR81u6' 

3 9rto 8Jf~ ~03 {).Oaf...{ 17Jol/l /..] S<o 1/rD ;; 5V I ;2<{~ ! 57 ! (0~ t.J I 

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.. ~'1-ff_ :227.~ ... _(!<{_ !f£L, ! 9 !J. "jj 857 ."?64 ~- Y/l!liP. 

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-···· 7. _:zi~.r-(}ul-1 /tfll~?f: __ -z .. ~_._ __ .£,_z ____ , _ _s;f.L __ 15"0 _ ... <£Y.9.---~~---··· 5Y _&;) __ (g_f i 

~ 9 L/D x& Y z cr;- o.wt.t , z&o , 1 : ~n , TD .~5{) ;;s-o '5)' ;U4 '(i? I 

s- '145""' 8ZJ. '-/ otf I n. (ba"f z~ /., 7 ~t'J /.]7 J'57 ;JSJ. ~ (l.l ~ 

4- 95"0 ?JJ~u)O{ I /J. {)()o 'f z&9 Ji7 5:o JL/7 PW ;2S7 l.ib {J) I;; 'I 

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I /00.) ~7,flo3 () tlt.J<I 7. /e{R 1·7 . .:f:n I'LCf_ ,;15/) ;1St; .~ Cos- ~3 I 

I - ·' 

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-~:.:--._"'· ··.:..' ,.... .... ... ~ ·: i' 

•<"-
!'·· l· . r·:·:,.:., 

:~.~·,_ 

i '. 

TEST ,.-In·c.~·--~. 

Me~ f\-l.; Sampling Data 

· . . · • Comments:. 3 t· ,i.f f5 '2. (~ '-1 'l 

• ,? "-ll, 1..o'l <? -~ 1 

'3. ), '1J '(;} 6 l. 

Projt!ct # 1 G 5D Meter Box # . 1. 0 ( 0 

,, Pt.mt-F-~·l. ~ 1\ · Meter Cal. (Y) I a {) '2.(1'] 

Unit/~tack ~ "Q Pitot Cal._(<t:p) 0 /SL.j 

%C02 . O,D:3' 

%02 )-i.'l, b 

%CO 

Op.eratpr "\1) R ?'N~z~~ # _ %N2 ')C, .J) 

Run # ~ Nozzle Dta. (m.) ', l,) Assumed Moist % __ _ 

Date· '0.,.. \ j- 1'3 Stack Dia.{in.)t Final.Moist.% --- Sample Tirne _a_,_ljQ_~_;___ S1atic'~ress,("Hg.) ______ Final Isokinetic% ---::---

->~· Min/pt IV'/£' Bar. Press. ("Hg) '1. c,, I ;,::tialLeak Rate---=-.......__ 

Filter# I \ --Leak Check Vol. F ina! Leak Rate 

Orifice Vacuu 

Port/ 

Imp. 

1 

2, -

3 

4 

5 

6 

' ' \ 

-----~------ ~ 

! 

.· 
TEST, Inc. !Comments: ''I~ V\1\. k' t.q l ~ Sampling Data L---------------------------------------~ Project # I 5'. s:- (J Meter Box # __ _ %C02 

,. --- Plant F (! i V"\ e,.;./1 Meter -cal. (Y) --- %02 ----'--

Unit/Stack -i;\: 5" IJ "·ii~.Uvt.S.f PitotCal. (Cp)_,..----

Operator {l ft ,..J Nozzle#----'-

. %CO ,. ----- %N2 __ _;.. 

Run# ?.... A- Nozzle Dia~ (in.) Assumed Moist% --- Date ·~ /13 /tl ··· Sta~k.Dia.(in.) ___ _ 

Sample Time ').,.1--j d · Static Press.("Hg.) · Final Isokinetic% 

Final Moist. % ----'---

Minlpt i l) i 5 Bar. Press. ("Hg) Initial Leak''Rate ~. · 

Filter# 1 D i Leak Check Vol. 

Port/ 

Point 

\ 

Dry Gas Pitot 

Time Mete.rJs:;F) 

1 

--- Final Leak Rate 

V acuu ' Stack Prob;e 

Rate m '. Temp. 

(F) 

< 

. ·~ 

.,., .. 

Imp. Initial 

1 

2 

3 . 

4 

5 

6 

cfm@ --- cfm@ 

Filter 

Tenip. 

(F) 

-~ ............ ~""'--""->- -~.. ;g... .:..(::_~~!2.-;:;.:. ~~- _:_~~~- .. ~~~--··---

Final 

"Hg 

"Hg 
!

Comments: 

_ _.:____::....=.__~.:......:;_ ___ Sam piing Data '---------,-----~------~-------' Meter Box#~ o \ o 'l"'"~~ %C02 6 _.:] Imp. Initial 

Meter Cal. l 06,,\{ (Y) \ .il~c-1: %021-0,(.r) 1 

Pitot Cal."(Cp)~.~- %CO 1 

Nozzle# %N2 }t; _·l. 3 

Nozzle Dia. (in.) _h-5 il Assumed Moist% . . · $(; 

Stack Dia.(in.) .. -- Fimil.Mois{% 5 ~ -'----+------

Static Press.("Hg.) tY~ I Final Isokinetic % ___ ____,.._ 6 ...... __ \ ___ . 

. Bar. Press. ("Hg) d-"1\·~ '5 Initial Leak Rate , (){)t:J cfm@ 

Filter# Leak Check Vol. Final Leak Rate D cfm 

iO "Hg 

s 

Pitot Orifice Vacuu. 

Velocity· Press. 1-------lf------.....:.__~ 

"HlO) ("H20) 

r 

I . , 

! 

t 

r~,,~" f--~--+~-=:.--=---r~-!~..:::...:~~:::::=:::..~[-£~~-J.....:...::_:__~~-...:L---:.j..:...::J.~~-L.;:J~!:!':~--~::!-:L-!-·.LL..::..".~IL:!-!.~....li.;.Lj 

r· 

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j 

'1 : 

i 
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TEST, Inc. kOmments: 

0107(;" /fLAre..,..$ Sampling Data 

Projecl# ! 5 t;; () 

~;.mp'#J '.t:1/FfPI.d 

· · Plant ,p e.-l u'IACAA 

Unit/Stack ~ i {J H 

Operator C...~ 11Y\ 

Run# I 

Date ____,._3--.l-1 5-/.-t~l--

Sample Time_---~,.\ -:::1."-'0""-----

Minlpt ~ 

Filter# 

Ptirt/ 

i 

Meter Box# J..c::~t06"'.-ttSt" 

Meter Cal. (Y) L ,o 3D:h 

Pitot Cal. (Cp) D d5 ':f · 

%C02 tJ, 'i Imp. 

%02 ,IJ?os-

%CO --- Nozzle# %N2 --- --- Nozzle Dia. (in.) [t 5 Assumed Moist% __ _ 

Stack Dia.(in.) __ _ Final Moist. % --- Static Press.("Hg.) NIA Final Isokinetic % _____ _ 

Bar. Press. ("Hg) Initial Leak Rate ---- ~~~ 

Leak Check Vol. Final Leak Rate 

Orifice Vacuu Stack Probe 

Press. Rate Temp~· 

(F) 

2 

3 

4 

5 

6 

~- l---____,~~~!1-f,.£.1._--fl"-!-~~~~w...L.L........f--'!....__~../---t-JL-:~~~~---~LE.f__~ ;.,jf· ~-·~_" ___ __,_ __ ___._ ___ __._ __ ___, __ ...;_.j, __ ____. __ --~... __ ___~ __ ___~ __ --l... __ ___I_-'-.L_...J 

l 
·• 

~: 

' 

TEST, Inc. 

fJ ~t> ;t"'"' ffiJVO..,..S Sampling Data 

Comments: .)).55-f@ SS 

J).J,{'B ' { 

Project # · . I 5 f 0 Meter Box # e?OI 0 %C02 o, 't 

4.'1 . d L-j .r ~ ') !>-

]C),'))re ~£ 

Imp. 

Plant. F~t .... ~ Mete(_ Cal. (Y) /,@Qj %02 ~ s-' l 

Unit/Stack ~ 1*_1) a H Pitot Cat' (Ep) D.£ '1 %CO___ 2 

Operator 'B:K . Nozzle# %N2 _ ___;_' _. 3 

Run# ").. Nozzle Dia. (in.) .I~ f) Assumed Moist% 

Date___.!::J;f·-( 5--/,.....,·t ...... J___ Stack Dia.(in.) br;f: Final Moist.%---

Sample Time t 1. C) Static Press.(" J-Ig.) Final Jsokinetic% ---

4 

5 

6 

Min/pt . f Bar. Press. 1.." Hg) d_q'. or lni tial Leak Rate ,OOL cfm@ o "H. . -,,o g 

Filter# Leak Check Vol Final Leak Rate cfm@ "Hg· 

· Dry Gas Pitot 'brifice Vacuu Stack Probe Filter Imp. Dry Gas 

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

Point '/'30 . ln15?;ool ("H20) ("H20) (cfm) ("Hg.) (F) (F) (F) (F) In Out 

3- ~ l/!3s- ·lu/IJ. 1cY(b ().OO{)Lt i 7 .lfs:-(9 .;;:'/) 137 t?l'-lfl ,?lSb /,67 7t!_ 73 

7 1 '-lo lfp!Lj o/()..J /} {)()(){_{ . . I 1 /ldb 5:'0 J -~0 :255' _.;?51 .. {pg/ /Ptt 71 

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) /.S"D It g.J-/ Jt 7tJ7! (), 0004 l1 , :1~{, ~iJ I? I ~57 ;JCI(j' tp_f( i[£( i&&, 

't I s~_l/.;Jl, '-l~l tJo/rrJ<J . LL., 7&1P s::o / ?fJ ~.)\ . ;;tsJ {/I) ~ 

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Certified Accuracy± I 0%, Traceable to NIST 

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0 High Flow D COIL 

D Static Prefilter D AGS 

[81!85 mm 

Type ofTrap: 30/5 

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0240mm 

0300mm 

0450mm 

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Date/Time e, 1 as 

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• 

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Chain of Custody 

Date: ··z · i · I 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 
EX 

Sorbent Trap 

Chain of Custody 

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.cl- ;-)._ Boiler ID: ~ \ :> '(\ <-~ n (· \_~~) 

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Certified Accuracy± I 0%, Traceable to NIST 

Spike Date: ___ _ Spike Time: ___ _ 

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Sampled By:_L..;;:; ... ;...;·)~C)_.· ---------

Test Start "?> ·· t ;..\ -1; 

Date/Time : 6 v. <t 5 

('I; 

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QA/QC Signature (Spiker), ________ _ 

0 High Flow 0 COIL 

0 Static Prefilter 0 AGS 

181.185 rnrn 

Type ofTrap: 30/'5 "\-t'i·\?~ 

Test End , ~C)\ \\ '/1~ 

Date/Time 

0240 rnrn 

0300 rnrn 

0450 rnrn 

Date Time ~Temp Sorbent ~Rate Dry Gas Meter Dry Gas Meter Total Volume 

'VI'f 0E or 0C) ~~emp in) Liters Initial Liters Final Pulled 

r°C) 

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Chain of Custody 

Date: ; t -- t - 1 ) ----------------

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 

T . ., l (....__ est Locatwn: C~c. v 1. \I(_ --~~~~~---------------

Trap ID: OL /5 b D (; L( 

D Spiked At: 

Certified Accuracy± 10%, Traceable to NlST 

Trap @ B (Circle One) 

QAJQC Signature <TrnpMok~~-

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 

[8ll85 mm 

0240mm 

0300mm 

0450mm 

Sampled By:_C._)_~_· _rY'_\ _______ _ Type ofTrap: ____ 3_0_;./5 _____ _ 

Test Start ~- '· "t- l 3 

Date/Time : 1 -;7 • :; 0 

Date Time ~Temp QfoC) 

3f\i)-- .! .;)...:>..;;;..- _i,,;;l ';, 

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Sorbent 

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Date/Time 1 '1 3:::? 

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Pass/Fail e 3 

Flow Rate Dry Gas Meter Dry Gas Meter Total Volume 

~in) Liters Initial Liters Final Pulled 

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Relinquished by Tech.: __ _,_·· L..-~ __ '·_" _--:."--.~-~ _,. _-.--'.""'.\'-, --'-----'-)-'::_,_?-=;._='· --..=:.·-''~· (=··:_:(_/ ________________ _ Date: _______ l_-__ ·; _-::_. __ _ 

Received by: ___________________________________________________ _ Date: ______________ _ 

Relinquished by: ________________________________________________ _ Date: ______________ _ 

Received for Laboratory by: Date: 

. I 

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 
~EX 

Sorbent Trap 

Chain of Custody 

Test Location: C_-e /tt ~ :- -=~~~L----------------

Trap ID: OL / 5 b 0/ cf 

Trap A m (Circle One) 

IZJ U nspiked D SpikedAt: 

Certified Accuracy± I 0%, Traceable to NlST 

QA/QC Signature (Trap Maker)~ ~//~ c:;7/---

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 

181.185 rnrn 

0240 rnrn 

0300 rnrn 

0450 rnrn 

Sampled By:.....::...C ....... t>~f_VJ....} -------- Type ofTrap:. ___ ~3....;0;;......:...;;;6 ____ _ 

Test Start j - 1 4 · 1 3 

Date/Time : i o- ·, 1 0 

Leak Check1 c.JlO 1 

ail CS ?> 

Date Time ~Temp Sorbent 

roC) ~~emp r°C) 

'?J/li \Ql-:,0 ~;).\. ~ ;t-:>C 

\.~so t-e3t -~ c.;c 

J/ ti t"3.10 I\ J- do<:) 0 

7> /( '1 i 3"3 0 \ \ 9.. :;~...;u 

3 /11-f I j S"G l \ '1. :7 '-iD 

3 ;, /;( 1"1! 0 I ;l~ ~L:.;Q 

i"i 30 \ l ~ 95-0 

J Total/ Average 

Test End J - t "-(.- 1 J 

Date/Time I hf. ; JO 

Leak Check , cc t 

Pass/Fail e q 

Flow Rate Dry Gas Meter Dry Gas Meter Total Volume 

@in) Liters Initial Liters Final Pulled 

tr_-CO o.ooo <3 I <::,"IS 

1..-{e:, ·; -s (::i"'i 1 l-'~=-,o 

i.fCG 1l.b"10 :) (:,, ;J (, :;-

L~oo )c,,ji,') );), 3.90 

L(00 5 s·.)::.-:.:: ~'-i r·£-1< ..: .... : it.._...' ..t 

.C.tC(_,") '"IJ.i '04':::. S-?.fc. I "7 

:..lOt> 'S"d .~1-1 

Chain of Custody 

Date: l-t - l - l 3 

Received by:. __________________________ _ Date: _______ _ 

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 

' 
EX 

Sorbent Trap 

Chain of Custody 

Plant/Source: Fe. { 1Y'<2\ {\ Test Location: C.e r\ t e'f'....._ ----------~~-------------

Boiler ID: ·~ tf~ ~ \\Vt?'S t'. ~<:) 

Dunspiked 

TrapiD: fb f5077? 

Trap = BCircle One) 

QA/QC Signature <TrnpM"'~J~ 

Spike Date: 2/ti//3Spike Time: /'l/0 ~~~/ QAIQC Signature <S~/ 

0 High Flow 0 COIL 0 240 mm 

Estimated Hg in Section I : ______ --=n~g;;>.. 0 Static Prefilter 0 AGS 0 300 mm 

gj 185 mm 0450 mm 

Sampled By: __ G_· '2>_-_'("V) _______ _ Type ofTrap:. ___ ...;;;3CJ-=-6~~::::;..... _____ _ 

Test Start ;) - l~..l. '" 13 

Date/Time : 1 5•- 0() 

Date Time ~Temp or 0C) 

3 li·~-- 1f0.0 t-A 

i 'l) _") J} it'l 

3/;t-j i5'io • ,;l(o 

j /ttt (ioUO t,;;) 0 

3jl~ tbd.:.:) { '3 t 

d ;,~ \(.LtO i '3 '1 

''700 

I Total/Average 

Sorbent 

~Temp E or 0C) 

,;t~ \. 

.~':\0 

a-s-o 

:;-su 

..2 -:)(,') 

&<5-o 

Test End ·Z>- I. '1' ·- ( 3 

Date/Time I ·1 :. o o 

F~ate Dry Gas Meter Dry Gas Meter 

in) Liters Initial Liters Final 

t..t.C'C' o.-0DU <;:; "·l J., "3 

YCO ~. l.Y::\ \''1' ~~) 

'toe 11. '?'t5 :/7. "l'iO 

4,00 '3-t,£'10 :_)" ..... )'1 -1!) \. . ..-.0 

iiOO 3-{ .·)20 ·-i t..j. 3'1 ') 

'-i,tDO '-j '-{ I '3 o, I) "5'1· (?\<? 

4.0(.) 5 '"i, <::, \ ""'~ 

Chain of Custody 

Total Volume 

Pulled 

Date: /..i ·- i ~ t 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 

Barometer 

PreTest Y 

29.4 Date 

1.0203 Calibrator 

04/02113 

csm 

Po Vac Vw Tw Vd Td y 

"H20 "Hg ft3 °F ft3 °F 

•·•••·•••• \ \ ••... 0.000 60 720.339 60.5 •••••••••••••••••••••••••••••••••••• 0.5 10.000 61 730.16 62.5 1.0189 

ntN < &g• 1o.ooo 60.5 9.821 61.5 

> 

••• H • 1o.ooo 61 730.16 62.5 

1.00 20.000 61 739.955 63 1.0218 

:; ~ygl. 10.000 61 9.795 62.75 

•••••·• 20.000 61 739.955 63 

1.50 30.000 61 749.72 63 1.0242 

<:/AvK 10.000 61 9.765 63 < •• 

•••••••• •• • 30.000 61 749.72 63 illill2 

2.00 40.000 61 759.505 64 1 0218 

~:;::··¥···•·#.:¥~!s# .. ,·~·~~~·*====*=~~~~:~o~o='=~~~~ =*==7~59·~~.~~~=5 ='==~:;;..;.;4·~==1+.4- 2.50 50.000 61 769.38 63.5 1.0117 

/ 

·~~8,(1\yg~ 

/ • 50.000 

10.000 

61 

61 

769.38 

9.875 63.75 

63.5 

~ 

~=3."""oo==+-----+--6-o.-oo_o_+-_6_1_--+-7-79_.2_1_5 -+--6-4-- 1.0145 

Average Y = 1.0188 
Barometer 29.4 

PreTest Y 1.0468 

Po Vac 

"H20 "Hg 

~:::::::: 0.5 

:) 

1.00 

,•: ) 

1.50 

2.00 

2.50 

3.00 

Dry Gas Meter Box Calibration 

MeterNo. 2010 

Vw 

fP 

0.000 

10.000 

10.000 

10.000 

20.000 

10.000 

20.000 

30.000 

10.000 

30.000 

40.000 

10.000 

40.000 

50.000 

10.000 

50.000 

60.000 

10.000 

Tw 

op 

57 

58 

57.5 

58 

58 

58 

58 

58 

58 

58 

58 

58 

58 

58 

58 

58 

58 

58 

Date 

Calibrator 

Vd 

fP 

174.528 

184.295 

9.767 

184.295 

194.105 

9.81 

194.105 

203.89 

9.785 

203.89 

213.625 

9.735 

213.625 

223.565 

9.94 

223.565 

233.433 

9.868 

02/20/13 

csm 

Td Y 

op 

61.5 1.0305 

61.5 

61.5 

61.5 1.0237 

61.5 

61.5 

61 1.0245 

61.25 

61 

60.5 1.0275 

60.75 

60.5 

61 1.0051 

60.75 

61 

61 1.0117 

61 

Average Y = 1.0205 
Barometer 29.3 

PreTest Y 1.0342 

Po Vac 

Dry Gas Meter Box Calibration 

Meter No. 2010 MST 

Date 

Calibrator 

Vw Tw Vd Td 

"H20 ·~ ft3 op ft3 op 

•••••••••••••••• 

1 0.000 74 840.515 74 

0.5 1 10.000 75 850.28 80 

10.000 74.5 9.765 77 

2 0.000 75 850.28 80 

1.00 2 11.000 75 861.06 83 

:liN • lf:gl 11.ooo 75 1o.18 81.5 

·•·•·• ··••••• 3 0.000 75 861.06 83 1.50 3 10.000 75 870.9 84 

n &g; 10.ooo 75 9.84 83.5 

10/05112 

csm 

y 

1.0276 

1.0302 

1.0285 

•••••• 4 0.000 75 870.9 84 ·•·•••• 

2.00 4 20.000 74 890.575 86 1.0313 

3.00 6 10.000 74 910.258 86 1.0336 

Average Y = 1.0302 
Dry Gas Meter Box Calibration 

Meter No. 2010 MST 

Barometer 29.35 Date 

PreTest Y 1.0302 Calibrator csm 

Po Vac Vw Tw Vd Td y 

ft3 op ft3 op 

1 0.000 66 322.792 71 

1 10.000 63 334.735 71 

64.5 11.943 71 

63 334.735 71 

63 344.685 71 

10.000 63 

4 0.000 63 

2.00 4 10.000 62 

62.5 

5 0.000 62 

2.50 5 10.000 62 

6 0.000 62 374.45 

6 10.000 62 384.338 

10.000 9.888 

Average Y= 1.0205 
CHEROKEE INSTRUMENTS INC 

30B Hg Dual Console 

Meter Box Post Calibration 

Cherokee#: 3620 

Meter# MI-Dual Hg Date: 03/05/13 

Serial#: DB 308-1110-2017 Barometric Pressure: 29.73 in.Hg 

HgSide 1 DRY GAS METER VOLUME 

Flow Time Initial Final Total Temperature ("F) Initial Final 

f!nm} (minutes) (Liters) (Liters) (Liters) Initial Final (Liters) (Liters) 

0.25 40.0 0.00 10.19 10.19 84 85 17883.00 17893.00 

0.50 42.0 0.00 21.72 21.72 82 83 17859.40 17881.50 

0.75 31.0 0.00 23.24 23.24 80 81 17831.20 17854.70 

HgSide2 DRY GAS METER VOLUME 

; Flow Time Initial Final Total Temperature ("F) Initial Final 

f!nm} (minutes) (Liters) (Liters) (Liters) Initial Final (Liters) (Liters) 

0.25 40.0 0.00 12.22 11.52 78 82 17731.80 17742.60 

0.50 35.0 0.00 18.07 18.07 80 82 17745.70 17762.80 

0.75 35.0 0.00 27.17 27.17 82 84 17770.20 17796.30 

Calibration Gamma (Y)* =I 1.0092 I 

Meter I 

1.002 

1.035 

1.023 

Deviation 

-0.018 

0.015 

0.003 

Operator: J McK 

Vacuum: 0 in.Hg 

CALIBRATION DEVICE VOLUME 

Total Temperature (°F) 

(Liters) Initial Final 

10.00 78 78 

22.10 77 78 

23.50 78 78 

CALIBRATION DEVICE VOLUME 

Total Temperature ("F) 

(Liters) Initial Final 

10.80 76 78 

17.10 76 77 

26.10 77 77 

Meter2 Deviation 

0.951 -0.013 

0.962 -0.002 

0.979 0.015 

Av.,.,.,Gamma~ l.fl20 I Ave<geGommF 0.964 I 

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 

w 

1- SAMPLE DESCRIPTION d d Vi 

z 0 z (INCLUDE MATRIX) c.. ~ w w ~ co 

z ~ ~ <( w ::> 0 0::: 1- 0::: 0 i= u l!) 

1 1 3/15/2013 Baghouse #5 Run 1 Back-halfRinse H2S04 

2 2 3115/2013 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 

(,/) 

0::: 

w LL Z '0 

0 <C :c 

# 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 ! 

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 0 Vi 0 0 z z a.. (INCLUDE MATRIX) 

::E w w ::E CJ 

z ~ ::E <! w :::> 0 0::: 1- 0::: Cl i= u ~ 

1 1 3/13/2013 Baghouse #5 Run 1 Filter 1012 

2 1 3/13/2013 Baghouse #5 Run 1 Front-half Rinse 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 3/13/2013 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 

oi-l 

Cll 

~ 

II) Cll 

0::: c. w u. z :E 

~ 0 <( 

=1:1: 1- ~ z 0') 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 

LU 

1- SAMPLE DESCRIPTION d Vi d 0 z z (INCLUDE MATRIX) c.. co ~ LU LU z ~ ~ ~ <( LU ::::> 0 0::: 1- 0::: Q i= u (.!) 

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-half Rinse 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) 

:;E 

V) Q) 

0::: a. LU ·.;; u.. z ::I 0 <C :;E :tl: 1-

z 0'1 0 N u :;E 

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 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 

u.J 

1- SAMPLE DESCRIPTION d Vi 

z d 0 z c.. (INCLUDE MATRIX) 

:E u.J u.J :E co 

z ~ :E <( u.J :::> 0 cr:: 1- cr:: c i= u (,!} 

1 1 3/27/2013 Blank Filter 

2 1 3/27/2013 Blank 5%HN03/1 0% H202 

3 1 3/27/2013 Blank O.lN HN03 

4 

5 

6 

7 

8 

9 

10 

...!:!! 

"' -1-' 

Q) 

~ 

V) ~ cr:: c.. u.J ·.;:; u.. z :l 0 < 

# 1- ~ 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 

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 v; 

2 0 2 c.. (INCLUDE MATRIX) 

~ w w ~ cc 

2 ~ ~ <( w :::> 0 0::: 1- 0::: c i= u (.!) 

1 1 3/15/2013 M23/PCB XAD Trap #7, Baghouse#5 Run 1 

2 1 3/15/2013 M23/PCB Filter, Baghouse #5 Run 1 

3 2 3/15/2013 M23/PCB Trap #1, Baghouse#5 Run 2 

4 2 3/15/2013 M23/PCB Filter, Baghouse #5 Run 2 

5 3 3/15/2013 M23/PCB Trap #6, Baghouse#5 Run 3 

6 3 3/15/2013 M23/PCB Filter, Baghouse #5 Run 3 

7 1 3/19/2013 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.. 

...... V) 

c: 

rtl 

.... 

:::J 

u.. 

...... V) 

c: 

·x 

0 

i5 

co (,/) N 

0::: -::1" w r:c u... 2 ~ 

0 <( <( 

:t:l: 1- u 

2 ("'') 

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 

I 

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 

w 

1- SAMPLE DESCRIPTION d d Vi 

z 0 z c.. (INCLUDE MATRIX) al ~ w w z ~ ~ ~ <( w => 0 0:: 1- 0:: Q i= u l!) 

1 3 3/19/2013 M23/PCB Trap #3, Baghouse#2 Run 3 

2 3 3/19/2013 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 

s:: 

ro 

,_ 

~ 

u.. 

.......... Vl 

s:: 

·:x: 

0 

Ci 

00 

V"l N 

0:: 

w "'" r:c u... z c:: 

0 <( <( 

=1:1: 1- u 

z N') 

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 

1- SAMPLE DESCRIPTION d d Vi 

z 0 z (INCLUDE MATRIX) a.. r:o ::iE w w z ::iE ~ ::iE <( w :::l 0 0:: 1- 0:: Q i= u ~ 

1 1 3115/2013 Baghouse #5 D/F/PCB Run 1 Front-half Rinse 

2 1 3115/2013 Baghouse #5 D/F/PCB Run 1 Back-half Rinse 

3 2 3115/2013 Baghouse #5 D/F/PCB Run 2 Front-half Rinse 

4 2 3/15/2013 Baghouse #5 D/F/PCB Run 2 Back-half Rinse 

5 3 3/15/2013 Baghouse #5 D/F/PCB Run 3 Front-halfRinse 

6 3 3/15/2013 Baghouse #5 D/F/PCB Run 3 Back-half Rinse 

7 1 3/19/2013 Baghouse #2 D/F/PCB Run 1 Front-half Rinse 

8 1 3119/2013 Baghouse #2 D/F /PCB Run 1 Back-half Rinse 

9 2 3/19/2013 Baghouse #2 D/F/PCB Run 2 Front-half Rinse 

10 2 3/19/2013 Baghouse #2 D/F/PCB Run 2 Back-half Rinse 

u 

c.. 

......... Ill 

c: 

ro 

'-

::J 

u.. 

......... Ill 

c: 

·x 

0 

i:S 

co V) N 

0:: "" w co u.. z 0:: 

0 < 

# 1- 6 

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 

w 

I- SAMPLE DESCRIPTION 0 0 v; 

z 0 z (INCLUDE MATRIX) w 0.. J:C 2: w z 2: ~ 2: <( w ::> 0 c:: I- c:: Cl i= u (.!) 

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 3115/2013 Train Blank D/F/PCB Front and back half Rinse 

4 

5 

6 

7 

8 

9 

10 

:J: tn <( 

c:: c.. w 1.1- z ""' en 

0 < N 

=1:1: I- ~ 

z c:c 

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 I 

Blank 

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.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 d Vi 

0 z z c.. (INCLUDE MATRIX) 

~ w w ~ tC 

z !;;( ~ <( w ::> 0 0:: 1- 0:: c i= u (,!) 

1 1 3/14/2013 PAH XAD Trap #5, Baghouse#5 Run 1 

2 1 3/14/2013 PAH Filter, Baghouse #5 Run 1 

3 2 3/14/2013 P AH XAD Trap #8, Baghouse#5 Run 2 

4 2 3/14/2013 P AH Filter, Baghouse #5 Run 2 

5 3 3/14/2013 PAH XAD Trap #1, Baghouse#5 Run 3 

6 3 3/14/2013 P AH 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 

:c 

V'l <( 

0:: c.. w ....... u.. z 0'1 

0 <( N 

~ # 1-

z co 

0 0:: 

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 

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 

w 

1- SAMPLE DESCRIPTION c:i c:i Vi 

z 0 z (INCLUDE MATRIX) 0.. a:! ~ w w z ~ ~ ~ <( w :::> 0 c::: 1- c::: 0 i= u ~ 

1 3 3118/2013 PAH XAD Trap #9, Baghouse#2 Run 3 

2 3 3/18/2013 PAH Filter, Baghouse #2 Run 3 

3 3/14/2013 PAH 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 V) <( 

c::: c.. w """ Ll- z 0'1 

0 <( N 

=1:1: 1-

z """ cc 

0::: 0 

u <( 

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 

LU 

1- SAMPLE DESCRIPTION d d Vi 

z 0 z (INCLUDE MATRIX) LU c.. co ~ LU z ~ ~ ~ <( LU => 0 a: 1- a: Cl i= u l!) 

1 1 3114/2013 Baghouse #5 PAH Run 1 Front-half Rinse 

2 1 3114/2013 Baghouse #5 PAH Run 1 Back-half Rinse 

3 2 3114/2013 Baghouse #5 PAH Run 2 Front-half Rinse 

4 2 3/14/2013 Baghouse #5 PAH Run 2 Back-halfRinse 

5 3 3114/2013 Baghouse #5 PAH Run 3 Front-half Rinse 

6 3 3114/2013 Baghouse #5 PAH Run 3 Back-halfRinse 

7 1 3118/2013 Baghouse #2 PAH Run 1 Front-halfRinse 

8 1 3118/2013 Baghouse #2 PAH Run 1 Back-half Rinse 

9 2 3118/2013 Baghouse #2 PAH Run 2 Front-half Rinse 

10 2 3/18/2013 Baghouse #2 P AH Run 2 Back-half Rinse 

:I: V) <( 

a: c.. LU ....... u.. z CT'l 

0<( N 

# 1- o;t 

z co 

l::t:: 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-'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 ci ci Vi 

0 2 2 c.. (INCLUDE MATRIX) 

~ LU LU ~ co 

2 ~ ~ <( LU :::> 0 0::: 1- 0::: C) i= u l!J 

1 3 3118/2013 Baghouse #2 PAH Run 3 Front-halfRinse 

2 3 3118/2013 Baghouse #2 P AH Run 3 Back-half Rinse 

3 3114/2013 Train Blank PAH Front and back half Rinse 

4 

5 

6 

7 

8 

9 

10 

:c V) <( 

0::: c.. LU ....... u.. 2 0'1 

0 < N 

~ =1:1: 1-

2 c:c 

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: 
APPENDIXG 

PLANT OPERATIONAL DATA 
3/13/2013

0

#5 Fce

Time Opened Time Plugged Tap Number Tap Weight Fines Usage Liquid Metal

7:35 8:00 971

9:30 10:30 972

11:30 11:55 973

1:40 2:05 974

3:45 4:30 975

6:15 6:50 976

8:30 9:00 977

10:30 10:55 978

12:30 1:00 979

2:35 3:00 980

4:40 5:05 981

6:30 6:55 982

Total LBS

Total NT

Note: Production and Raw Material data submitted separately as Confidential Business Information

With Fines

Raw materials consumption

Redacted
3/14/2013

0

#5 Fce

Time Opened Time Plugged Tap Number Tap Weight Fines Usage Liquid Metal

8:35 9:00 983

10:40 11:05 984

12:40 1:05 985

2:30 3:00 986

4:30 5:00 987

6:20 6:50 988

8:30 9:00 989

10:30 11:00 990

12:30 1:00 991

2:30 3:00 992

4:30 5:00 993

6:30 7:00 994

Total LBS

Total NT

Note: Production and Raw Material data submitted separately as Confidential Business Information

Raw materials consumption

With Fines

Redacted
3/15/2013

0

#5 Fce

Time Opened Time Plugged Tap Number Tap Weight Fines Usage Liquid Metal

8:35 9:00 995

10:35 11:00 996

12:35 12:55 997

2:35 2:55 998

4:25 4:55 999

6:30 6:55 1

8:30 9:00 2

10:30 11:00 3

12:55 1:30 4

3:15 3:40 5

5:30 6:00 6

Total LBS

Total NT

Note: Production and Raw Material data submitted separately as Confidential Business Information

Raw materials consumption

With Fines

Redacted
0 

\ 

r-::1 ~- ~, \. ... - ·._) 

~: ; y~; l 

Jo:oo 

lO.IQ 

1 t>: 3o 

10 ~ Lj5 

/fo 'I 

; l <., i I _., 

l1b ' . 

Jb8 

;rolo 

j(p3 

j(p/o 

. u/-1 

I l:oo 1~9 

1 J:J5' .. lt.uY 

. } 1.'5~ .. !lfi 

11 . Lf ~r .. , I ~I 

jd. ·. 0 b F .. l fdJ .. · .. . . _. 

l d. . IS t- .. J ~4 .. 

/J.~·3o t .. JGS .. _ .. 

i,;oo 

/.'I 5 

I ,. r 

t • ·' 0 . • • <J. . . ·•··· .. 

. llo 

/'J 0 

~ . ·- ..;. .. ·- . .. ~- ···-·- . . ·' .. . .. . -· -~--· ·-·--

·' 

._':;;::>: .•. ;;.. TffJ'P 

• ; i \ \ 

-: : -),. ' 

388.f.o 

3'90.8 

381.3 

.J-3-I.Io 

3 7/].'-/ 

-=<q'"2, u ._) ,...__~. 1 

3ffi. I 

4Q5. _!p 

jl9 ·--~~-· 

363.fe. 

'ltD. Z373.1 

38S. '-J 

J:-:((1" 

._;. / ~; ~ '_..,q 

u: ... ·) ! : _J .. -

loa% 

/(()h 

16o% 

;oo% 

.... _/(]_6 % __ /cp% 

JOO% 

... !rP% 

.... /ftJ% 

. __ )QfJ io 

_ ..... j_o o lu 

__ L9a ole 

o_ 

/Q()Io ····----··c--.•,-· 

.... 
til!liHet Ternpemhiln::: 

St21dk Ternpuatrunne: 

"IF 

Bag!!Jo<v;.§f Bllu'h' · 

Tra!llsffer imr!Jlwto· 

MAGNEHELJIC GAUGES, Oll1l Une J Cieanil!11g O~rn Ulllle 

Noll JHoppelf Pwessilll~re .t-5 '/z hdH20 ~· :t¥-InH20 No 7 Hoppe;r lP'l'"esslllln: ±_]_InlHhO 

No 2 JHoppeir PnesS!!l!lfe i .. "' .L __ hlii-llzO - ~hnHzO 'l 

No 3 Hopper P~ress!Ul;re tj /~ l!!llHzO '· 3' IJJJilH 20 

<4 -

No 4 Hopper PifeSSllliir<e L_lnlH20 

No 5 Hopper Pwessrunre + 1 I~rnlH20 

No 6 Hopper lP'iressll!llre i._']_IlllllihO _ 

No 8 Hoppe1r lP'weS§!lilre ~_I!iilH 0 

No 9 Hoppeir Pwessilllne __ L_InHzO 

NolO HopperlP'ressi!!lwe_l __ hnH20 

No t i Hopper lP'n:ssamf· __ J __ KnllbO 

( 

Bags 

Cleaffiling 

--_ -\~~~. _ fll1llHl 20 

: !Jl1lf-h0 ---r-

'\ hd-l[z 0 --T-

- t .fflfiH20 

' Ilf!H20 ·-------!-·-

On/Off 

Screw 

Convevollr Missing 

No 1 Hopper 

No2 Hopper 

No 3 Hopper 

No 4 Hoppe;r 

No 5 Hopper 

No 6 Hopper 

No 7 Hopper 

No 8 Hoppeir 

No 9 Hopper 

No 10 Hoppew 

No It Hopper 

EQUWMENTPROBLEMS ____________________________________________ ~----

MECHANICAL WORK PERFORMED ________________________________________ _ 

COMMENTS: 
.. ! 

. .-.. "•.: 

femperilllig Aiw If,"1fq:r 

Inlet Temperature 

Staclk Temperatur:e 

No 1 Hopper 

No 2 Hopper 

No 3 Hopper 

No 4 Hopper 

No SHopper 

No 6 Hopper 

No 7 Hopper 

No 8 Hopper 

No 9Hopper 

No 10 Hopper 

No 11 Hopper 

On/Off 

----·---

~ ~ ~'(r . , .· ·.· r 

"F 

OJF 

. 18_ O_!_.L OF 

Screw 

Conveyor 

>:·ii ~'; 

.; F\ fU~li. ·,, . ~ :f !iJH, ~F-. •~ ;;,-:,;_,.',_ 

Baghm!ise BRow<.:: 

Transfer Blowew~ 

Air PressMre: 

Rotary 

Lock 

-~· f L. -/_.~. 

PSij 

Cleaning 

__ j_L/ _ [nHzO 

! lnH20 ---r----

__ ( ::::~ ---+- . InH20 

Bags 

Missing 

EQUWMENTPROBLEMS ______________________________________________ ___ 

MECHANICAL WORK PERFORMED _____________________ -.,--

COMMENTS: 

''· 
-\.o··-~s 

i' t'mperi~g i~.ir Tem~; 

~:nilet! '1f,~mpemhi!rre; 

-:·}F' 

'JF 

~, 

ii f: (--,. 

l:l\2igihlo!liSif: mow,;; 

Trr2ilillStfN l!Ur.l>werr· 

MAGNEHJELIC GAUGES Oiill Liilile I Oealliihng Ollll Li1nl\e 

No l Hopper Pwessll!lre :___ia__ llli1lH20 -· 'f2. halH[zO No 7 Hopp<etr P~ressl!l!lrte ~ __ ln!Hl 20 

No 2 Hoppew PressiiJlre --;-5 IllllHl 20 - -\( 2.. llnH20 No 8 Hopper l?wessliJire ___, __ hnJHhO 

No 3 Hopper !P'~ress\Un: .+L)'),.f !ill!H20 . 3/4 !IDJH20 No 9 Hopper lP'ressilJJre ~ __ Il!llH20 

No~ Hopper l?wessrunre ±__]_lrnlH[zO _iy_InH20 No WHopper l?~ress!l!!Pe_,_HilllH20 

No 5 Hopper l?we§SI!lire + 1 _ !ililHzO .i.:L_ inHzO No ll Hopper lP':ressmre __ ' ___ lllltfhO 

No 6 Hopper lP'res§llllire ·1 ~ l!!lllH!zO __ 'J.-Z..._hnHzO 

Ciealllling 

·-__ 'l_:L_hr&iizO 

---~-----[lllllf-hO 

--L--hl&Izo 

' -~ __ InH20 

\ !nH20 ---,------

' 

Oll1l/Oflf 

Screw 

Conveyor 

Bags 

Missing 

No 1 Hopper 

No 2 Hopper 

No 3 Hopper 

No 4 Hoppe;r 

No 5 Hopper 

No 6 Hoppe!r 

No 7 Hoppeir 

No 8 Hoppeir 

No 9 Hoppe~: 

No 10 Hopper 

No ll Hopper 

EQUIPMENT PROBLEMS ________________________ _ 

MECHANICAL WORK PERFORMED ____________________ _ 

COMMENTS: 

~ 
~i1.m!i:'. 

Oat~;: 

r~mi:. : ·---' 

Tempeiring Air Temp: 

Inlet Temperahu·e; 

Stack Temperatrunre; 

"JF 

MAGNEHEUC GAUGES On Line 

No U Hopper Pressl!.ilre+ (p !llllH20 

No 2 Hopper Pressure +--) f,i !nH20 

No 3 Hopper Pressure ~InH 0 

No 4 Hopper Pressure + ..., InHzO 

No 5 Hopper Pressure LL_ InH20 

No 6 Hopper Pressure ·t -; InH20 

No 1 Hopper 

No 2 Hopper 

No3 Hopper 

No 4 Hopper 

No 5 Hopper 

No 6 Hopper 

No 7 Hopper 

No 8 Hopper 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

On/Off 

-~lnH 0 

--.i:LinHzO 

··JLinH20 

Screw 

Conveyor 

'~ab 

'.f:o lF1i!li \ ;! • '~ f''i!H. <E l E,m!fH7 

Baghouse Blower 

Tra!lls1fe;r Biowelf; 

Ah· Press~Are: 

Rotary 

Lock 

PSll. 

PSI 

PSa 

Cleaning 

- _j_tllllH20 

--i--inH20 

1 lnHzO 

rinH20 

j__InH20 

Bags 

Missing 

I 

EQUWMENTPROBLEMS ________________________________________________ __ 

MECHANICAL WORK PERFORMED ________________________________________ _ 

COMMENTS: 
-~ __j.. •. ~ 

j ' • 

/L; fi\ t_; ~-

! /' 

/ ~J :; 

_I_. '..:.- •• ; ·., 

.. I 

.· ,. I . . 

,, . 'I' If :, c 

' ·/_ -:rl~ !) .J ·'-

-:;::···! I _,~ 0 . I 

1 J:::~ (-? 

zt)7,b 

45:2.8 

LJJ74 

. 3rrr; \ 

374.) 

.. LJLfZt) 

itZ.Z 

'-/~/.; 

' 

'L .. ·--' ~ ~. ~~--~- :J) -:;)! 11-J I 

! --- ·' ·~ ... 

/ !'-,,.,,./: ..,,.~·' 

/ .. ·'·'\ / 

_./•j •• ' .• · 

!oo% 

/6:,;% 

;oo% 

;co% 

ltJo% 

Joo% 

loo% 

. !oo% 

;oD% 

1oo;£ 

Joo% 

. -~·-·--- . ..... 
"~ :a;nn f 

f)~r;ii; 

f'E rnn:r: 

Temperil!llg Ai.r Temp: 

nnlet Temperlllh.nre; 

Stack Temperature: 

No 1 Hopper 

No 2 Hopper 

No3 Hopper 

No 4 Hopper 

No 5 Hopper 

No 6 Hopper 

No 7 Hopper 

No 8 Hopper 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

On/Off 

'F 

Screw 

Conveyor 

. ;~ 

Snno 

!F) FuH, 0 /2): '/, FaP.lt (Ei EmpKJ 

!Baghm11se Blowe• 

Transfe1r Blower; 

Air Pressure: 

Rotary 

Lock 

PSI 

PSI -~·-----

PSI 

Cleaning 

~ ~~ hllHzO 

-+--lnl-hO 

J__inH20 i 

i InHzO 

-rJ__InHzO 

Bags 

Missing 

EQUWMENTPROBLEMS. ________________________________________________ __ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
3 __ _ 

._., j._ 

femperiiillg Air Temp; 

hnietr Temperat!!l!ine:. 

Stack Tempewatil!re: 

llbghol!llse BDowex 

Tmilllsfe~r Blowerr~ 

Air lP'reSSI!!1rre: 

lP'Sfi 

PSI 

MAGNEHEUC GAUGES O!IT! Line 1 C!eaurnillllg 01fU Lilllle CRemni_!!g 

No » Hopper Pressillln~t= (o hRH20 • '/) baH20 No 7 Jl-lloppew lP'1nesswre ..,..~7 '/1 hn!H20 -- ~~Y InH20 

No 2 Hoppe1r lP'wessilllre-51qzl!nf![z0 - \) z_ In!H20 No 8 ft-Hopper PnessMre ~.-' _h1lhO -. ~,_InlH[zO 

No 3 Hopper P~ressure_,__ l"/2 llmllfll20 - 3 /'-I lh:l1H20 No 9 !Hoppe!r Pressl!llre __jl__In!H10 _::{__hnl!-lhO 

No 4 Hopper lP'ressllllre: --7 lillllllzO - ~l!nH 0 No 10 !Hoppe1r P~ressUJwe-A-InH 0 _LinH. 20 

No 5 Hoppew Plres~mre "'tlhllfl\zO -. _j_i__IniH20 No 11 Hoppe1r PressmrellhtHzO { \ hilHzO 

No 6 Hopper PressMre_;_ / InH20 ~lnH[zO 1 ' --rNo 1 Hopper 

No 2 Hoppeir 

No 3 Hopper 

No 4 Hopper 

No 5 Hopper 

No 6 Hopper 

No 7 Hopper 

No 8 Hoppe1r 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

On/Off 

Screw 

Conveyor 

Rotary 

Lock 

Bags 

Missing 

EQUWMENTPROBLEMS ________________________________________________ __ 

.,< .· 

MECHANICAL~ORKPERFO~ED __________________________________________ __ 

COMMENTS: 

-

-:;?r~_.i~· 
f t(' 

f t' 

. L{ s ff(\. 

JDo f.({\. 

]· l ,- ~:) f, (1, 'i 

J_', L\S f. (fl. 

)',()!) f vn. 

i ( --·-

( ·0 ,:,:;; 

I f~ ~. I V ._./ 

/~9 

/65 

1~3 

I~ "J.. 

}(,5 

1~3 

.Lk~ .... 

. 207 0 ~ F 

_)f.__) ' 

-s~ t { 

tl{ 

c - ;_ 

Y~3.~ f 

39i.lZ)f 

0 

L../5~~7. f ... 

.!".- -· 

~cqO.b°F 

; r"' . ~_;;~ 

~ ,_,-' .... ,: 

)0.3.3 

I 03.3 

l 60.(, 

/03 3 

q t./.J 

. ... 
··'·:ijL 

'f. fu,F 

-;;·· .: 

:, -~ -~' 

l!~mperrirng Aftr lf :e!',r;p B~glH}!Ill§~ Bk·'f"i.';: 

~lllli<e11: Tempelf'!lltll.H'<:: 

St~clk Temperaturne:: 

TransfeJr BDOV<!'E r 

Air Pwessillu-<£: 

P'Sli 

! 0 '"'· PSI .... ,L.. ·--~ ·-·. 

MAGNEHEUC GAUGES On Line CDe~mullllg On Line 

No l Hopper PwessMire~_&_S_inH 0 _-=-l_InH20 No 7 Hopper PiressM!re i:J,_5 h»I-JhO 

Nfl 2 Hopper P~ressrume ~L !!nf_lzO - • 5 InllzO No 8 Hoppeir Pressilln: --=-h:aH20 

No 3 Hopper Pressmre+ S. S InH20 - I lnlH20 No 9 Hopper Pressam~ ~-= __ hnHzO 

No 4 Hopper PressMre4 5. S InH20 ~!!nlH 0 No 10 Hopper Presslll!re--=--lnH20 

No 5 Hopper Pl!"essmre ~ InH20 - • S InH20 No 11 Hopper Pressame --=-!!nH20 

No 6 Hoppe1r Pressure ~- (o hllH20 _:_LinHzO 

Screw Rotary Bags 

Clealllling 

- r illllH2o 

-=-lllllH20 

__ -:__lnH20 

-=-InH20 

InH20 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper ()iJ J J J 0 

No 2 Hopper ON J ./ .j 0 

No 3 Hopper orJ J J / 0 

No 4 Hopper otJ J ~L ,./ 0 

No 5 Hopper ON J ../ J 0 

No 6 Hopper otJ .../ / / c 

No 7 Hopper otJ J / v D 

No 8 Hopper 

No 9 Hopper 

No 10 Hopper - No 1 J Hopper 

"" 

EQUWMENTPROBLEMS ________________________________________________ __ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
I . ., .-- .\ ... ) :...; 

fempering A<i' J :ert\ J> 

lnitN Temper:JJlffij>r<:-

:St3lck Tempera~l.llir<t 

"F 

}~JO-el_"F 

:~H~ 

'f' f;_!!ij:: 

BaglhiO'Ill§t m~,J;" 

Translfer BHov;:•< :r 

Ailr Pressi.iln 

,( 

\ r lF"Sli _: ~·-

lPSR 

l_Q_Q_ rsg 

MAGNE.HEUC GAUGES On Lilllle CBeam\ng On Line CUeaurning 

No i Hoppu Pressmre+ 5 ,S_ in.HzO -_l_ill1lH20 No 7 Hopper PressM!re _ _t_L InH20 _-:_,S ___ hnH20 

No 2 Hopper Press1t111re ~lnH 0 

No.3 Hopper PressMwet~~-huH 0 

No 4 Hopper Pressure -~InH 0 

No 5 Hopper Pressure __ .±.]__ InH20 

No 6 !Hopper PressUAre __±]_In H20 

On/Off 

No l Hopper ON 

No 2 Hopper OtJ 

No.3 Hopper otJ 

No 4 Hopper f!H./ 

No 5 Hopper 01\l 

No 6 Hoppew OrJ 

No 7 Hopper otJ 

No 8 Hopper - No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

_::_,S InHzO 

- I lnHzO 

--5 lnH20 

~J.nHzO 

- .. lSinHzO 

Screw 

Conveyor 

,j 

./ 

/ 

,/ 

~/ 

/ 

/' 

No 8 Hopper Pressure ___ _:="_InH20 

No 9 Hopper Press\!.Bre ---=-hnH20 

No 10 Hopper Pressure-=-InH20 

NoH Hopper Pressure __ .':"'_lnllhO 

Rotary Bags 

- lnH20 

--·=-JnHzO 

__ -__ hllH20 

-~hliHzO 

Lock Chute Missing 

J J c 

J / 0 

,/ ... L (!) 

lL ~ 0 

./ ../ 0 

./ ./ 0 

/ .; 0 

-

EQUWMENTPROBLEMS _________________________ _ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
lo·oo A.m. 

\0 ·. \S A VI'\. 

i lo 

101 

ll \ 

f~l 

. -+.t .,.., ·-

~-, 

' --' 

' \I------

5 i c\c ~- \ e~f'\Y' 

() 

35Y B F 

0 

-; f ~- ~ - ~ i ..._,;, v t0 L/ U, 5 .. L F 

3S ~ .;;1..0 f 

\ 

10!3 

i03.3 

--~~----~- ---· .--- .. I o :5 .~ 

. "---- ··---- .. -~-

/OJ,7 

I o 3. :3 

_ \l ·.oo A rvi.! ~,.- _ . ll ~ .. · 

ll:ts A.m . • t·· ~ . Ill 

\60 

6 

3~LO f 

• ,,,,, • ~--, .. s,....,-~,.,.._..-..k ___ ,_.,.~-..,.~.._. ...... ••••••••' • "'" • 

{) 

314. 3 ~ ' ----··-~-------------- ..... l Q3 .J 

. . . . .•... , •. -'--~-----···· -------· -~ - .... - .. ----------·---~--~--~~- ·-----~- ........ ,__ ____ ~ .......... ~---~_,..,_ '•'J•• ----···········-----~4·---~-~,.,.---- ........ ------... ·---·-·-··"''~ ... d ................. _...._ ____________ .. ..,_ ----~-~-~-

-~ i --- --~ ·---- .. ············ -----·--- -----~------~ .. -----------~~- --. -···------···· ·-·--'~-- -..... 

': . . . . 

- -------~----~- ' ··+-+----~ .......... ·- ..,...,. ... __ .. ____ ... __ ...,-:.-~ .,_._.,_,_ ... ,,_,....,, .. .....,......-_., .. ~ ... -.. ~ -~~- __ ...... ..:_4 _________ , __________ ~-·- --·~--- --. ___ ; ____ ----..---.... ~~----------------~---~-~·-· ·-·''" ·~- ·---- ~~-~------~ .. -'""';_.,. 

! -- ·- ~·f ., . .,, ~·•• -.--·--•--·~-.···-·"''""'~~•-•··--·-·-~·----·-··-·--·-- ""-·.·w·• '"'"""-"""~-- ~----·-"-'"-•-•· ·~~~·-·~ .,. • & •··~•~_...,.__.._,.;J,. ___ ,_, __ , _______ _,_~,••--·•-··•-•.,·~· ·-•·••··~~--"·"-------<>.-.~--- _, 

' -J ' ; 

; l 
... ; ;~:. i~· ;. 

J'ef;lllj:>•uhtg A·ifr I em\!}. 

l:rnll<eli "f~mijpi<Pff>l![<H.£' 

§~llHt:lk T:empe;rah11rre: 

"1F 

3~do.:- 0 1F 

atd!gilHJ;\IJ1'3(e !Bnowe~ 

if :nJtlf!l§lf~;r Blower: 

~-

..; 

P§il 

rsrr 

MAGNEHELl!C GAUGES Oi!ll U!rnie Cle21!llillllg Ollll U~rue Cle~mnng 

No 1 Hoppn JPnss!lliir<e! S. '5 Iilllfl!zO _--::-1_ Kr.~H{zO Nil} 7 Hopi!Jle:r i?iiessrullr<e _: __ -::_ NlilllHlzO _:: __ , [)_ ll:~rulthO 

No 2 IH!oppe;r Pu·essi!Jir<e .±_LhliH20 - .. 15 lllllH20 

No 3 Hoppe;r i?ress!lme + .S. S lJ:niHl_zO ~-~ _I!nlHizO 

No 4l Hoppe1r lP'wessmre . +lllnH20 - .. S lnlHhO 

No 5 Hoppew lP'nessKnll"e _±_]_lllllH20 .,_. S lnlH[zO 

No 6 Hopper lP'nessll.lnr~ _±_lRllllH20 --=l_hnlt{zO 

No 1 Hoppew 

No 2 Hoppew 

No 3 HoppeJJ 

No 4 Hoppew 

No 5 Hoppew 

No 6 Hopper 

No 7 Hopper 

No 8 Hoppew 

No 9 Hoppe!r 

No 10 Hopper 

No 11 Hopper 

' 

0Jlll/0fjf 

ntJ 

01\J 

otJ 

otJ 

01\J 

ON 

0{\) 

Scnew 

Conveyor 

j 

/ 

/ 

/ 

/ 

/ ----/ 

N:(J) 8 Hoppe:r i?res1'aue -=--hllH20 __ -:_Jillllf-l[zO 

No 9 Ho!Jllpe;r lP'ness!lll;re __::_l!ll!!H20 __ -=-I!!lllHbO 

No w lH!oppu lP';ress!lllre --=-hnlH! 20 _---=:__ hnHzO 

No ll Hoppe' lPwessilllre _ _:::__ KllllH20 --=--I!!llf[zO 

Roaary Bags 

Lock Chute Missi!!llg 

-/ 7 0 

/ / 0 

./ / 0 

/ / 0 

v ./ 0 

../ / 0 

J / 0 

-

EQUWMENTPROBLEMS __________________________________________________ _ 

MECHANICAL WORK PERFORMED 

COMMENTS: DltW OOT I-1~01\)EHE. L\( 
,{ 

·' ... ·. 

Nam!:~ ---~-~.~---=--·- -~- \_:;;._,.: ..... 0__{:_:_~~--·­ Date. __ :;?_·J~ .. ;J _ Tirn.r.· _ c-i __ 19 --~- {Yj_, 

Tempering Aiil Temp. 'F 

InDe~ Tempen:nture: "F 

Stack TemperatlJllre: _3S.k.~ "JF 

.' ;_ ' 

,;.-c: ...... 

BaghoMse Blower 

T1rans1fer BRower: 

Ai1r Pressanrre: 

__ _ \.: :) ____ PSI 

PSI 

jOO ____ PSI 

MAGNEHELIC GAUGES On Line Clea~rning On Line Cle~mi~rng 

No 1 Hoppel!" Pressmre +- (.;. InH20 __:j__ lnH20 No 7 Hopper Pressmre ___:!]_ B:nH20 --:,S _inHzO 

No 2 Hopper Pressw11re __±_S__InH20 - .lS'InHzO No 8 Hopper Pressanre ____:::__lnH20 -=-Inf,hO 

No 3 Hopper Presswre _±_S_InH20 --=-l_inHzO No 9 Hopper Pressanre -=-h»HzO --=-InH20 

No 4 Hopper Pressure _±_]_InH20 - .S InH20 No JO Hopper Pressure__::_InfizO -=-InHzO 

No 5 Hopper Pressmre+_L_5_ InHzO -. 5InHzO No u Hopper Pressure__::_lnHzO -=-InHzO 

No 6 Hopper Pressure~ , 5 InHzO =-l_InH20 

Screw Rotary Bags 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper 6tJ ,[ ,L / 0 

I 

No 2 Hopper Ql\) J J ~ 0 

No 3 Hopper ON I ../ ./ Q 

No 4 Hopper f)(\) I ,/ ./ ., 0 

No 5 Hopper otJ J J ,/ 0 

No 6Hopper OtJ .L . ,/ v o· 

No 7 Hopper Qf\1 ../ J J D 

No 8 Hopper 

No 9 Hopper - No 10 Hopper --. 

No 11 Hopper 

,. 

EQUIPMENT PROBLEMS. ________________________ _ 

J1ECHANICAL WORK PERFORMED _________ ~-----------

COMMENTS: -------------------------------- •.. , 
; ·-~ .. 

:· r. e 1'/·. - ,., ~ i ~~~ ' ;; 7< ~ ;:. 

i 03 ) ·~ ·~- ~ v ' .... 

- f.:'( l~ I '1 .. , 0 ;. ~ 

- I. ~ \ ~j ' . l , a'. I D~. ~ I ---

" -~ .. :)() f ('Y'\ 16~ "<.Cf' ... t"'- v !b.,;. t loa. ~ 

I L{ \ '~l. c lo3. 4 "< !:J p rt1. Lj i f .._; 

u ~0 f Y'l\ /~2- '1.37' of JC5.S ' 

I Lf~S. --- 0 

1 i~ fyY!, 6\ J-; ~ IO~.~ 

f.f{\. \ b~ ~ l cr C{ 

0 

!J ·oo . ~ i \ \ f Cf5.l 

s: \.S ~.m. lbl ~~ 7. 0 7 F 9s .y 

s 30 f VV\.._ I 6ca 3 9Jfo. ~ 0f 9'-f. 7 

s ~ ll s '54 

0 

f.vn. 4J._Y.l r I ()3, ·····~· 

.2:>.. 

... ,. •· -.,~·~•e•-•- • "'' 

_, ....... .-... .. 
. . ';- '~ . ' ·.,I' -·~ . 

. f.: 

Date FUME nt 

Time; S -.: -· -· -· ... -

Tempuing Air Temp; 

hBiet Temperatunre~ 

Stack Tempell"atuw-e; 

Baghouse Bhllw<er 

Transfer BDow-er 

Air Pressure: 

PSH 

PS! 

. L)_Q __ PSI 

MAGNEHEUC GAUGES On Line CDeaning On Line 

No I Hopper Pressure + 0 InH!20 _-_l_InH20 No 7 Hopper Pressure ~=-inHzO 

No 2 Hopper Pressmre + S InH20 -. 75 InH20 No 8 Hopper Pressure _::-_InHzO 

No 3 Hopper Pressure.~; 5 S' InH20 _-_I_InH20 No 9 Hopper Pressure ___::_lnHzO 

No4Hoppe~rPressure ~s.s InH20 --.. S InH20 No lOHopperPressure--=:__InHzO 

No 5 Hopper Pressure ~InH 0 -.:) InH20 No II Hopper Pressure--=-hiiHzO 

No 6 Hopper Pressure ~inH 0 --=-L___InHzO 

Rotary Bags 

Cleaning 

-, S" lnHzO 

-==-InHzO 

---=-InHzO 

_::_InHzO 

--=-InlizO 

On/Off 

Screw 

Conveyor Lock Chute Missing 

No 1 Hopper ()tJ J j 7 0 

No 2 Hopper ON / / 0 

No 3 Hopper ()fJ ./ / 0 

No4 Hoppel!" o_tJ / ./ ./ 0 

No 5 Hopper aN / / 0 

No 6Hopper Ot_J L ./ / ·"" '-' 

No 7 Hopper 0 f\) ....,~/ / a 

No SHopper 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

EQUWMENTPROBLEMS _______________________________________________ __ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
T:empedi!!lg Anw Temp; 

R!!lllet Temnqp>enilli:IUire: 

"IF BaJgilllmnse l!Uowerr 

T~r~uilsfer Blowerr 

Air J?wess\Uln·e: 

, iPSK --·--- --·---

"IF 

Si:adk lfemperatillre: 

MAGNEHEUC GAUGES Oi!!l Lil!lle Cleallllillllg Oil11 Lfilffie 

Non Hopper lP'Iressl.ilu-e+S.S ll:llllH20 _::__l_haH20 No 7 Hopper JP'H~essmre _::_lKill.lHzO 

No 2 Hopper Pressame + S InlHhO -- .. 5 huH20 No 8 Hopper PresS\UlJre ~hlllH!zO 

No 3 ll-l!oppe1r Press\Ullre 1 S,S_Illllll-l!20 _::_LbilHzO No 91 Hopper Press\Ulne -=-JnHzO 

No 4 Hopper Pressuu·e ~ InH20 - • 5 llnlH!20 No 10 lH!oppew Press!lllire-=---hliHzO 

No 5 lH!oppetr P~ressmre ____:!:_]_ InlH!20 - • ') linlHhO No u 1 Hopper Pressmre----=--hnlH20 

No 6 Hoppe1r Pr:essl!llne + 5. S h11lH!20 -=-Ll!nlH!zO 

Rotary Bags 

PSI 

Clea!!lling 

,. \~ lllllllllzO 

-==-hllii[zO 

---=-hllH20 

O~rn/Off 

Suew 

Conveyow Lock 

J 

Chute Missing 

No 1 Hoppew OIJ j J 0 

No 2 Hoppew 0~ j / 0 

No 3 Hopper ON / j / C) 

No 4 Hoppew otJ / I / 0 

No 5 Hoppew otJ / / ./ 0 

No 6 Hoppew orJ j / / 0 

No 7 Hoppew ON / ,/ 0 

No 8 Hoppel!" 

No 9 Hopper 

No 10 Hoppew 

No 11 Hopper 

EQUIPMENT PROBLEMS ________________________ _ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
p,j~· Temp· 

I!li'H<e~ Tempew~ti!l!!fe: 

Stra~e:::k Temperr:BJ~iLme; 

PSK 

LO Q )p§ff 

MAGNEHJEUC GAUGE§ Oll1i U:rue CHe2l!l1ia!l1ig Orrn Ullll<e CHeaurnhng 

No ll JHlopJpll~:!r lP'ne§§Mre-\. lj._5 lh•H20 ::_-:__L __ htlt·lhO No 7 Hoppe:r lP'6"'<e§§ilil!ne _+_]_li!11iH20 - • 5 iulllHlzO 

No 2 Hoppe~r lP'wesstuJwe + S llnHbO 

No 3 JHoppew lP'nessllllre -+S. S JlniHhO 

No 4 Hoppe!r JP'ressure-\-5.5 h:~JH 0 

No 5 HoppHelf Pw<e§§IUIIre -t l llil1llf:l{z0 

No 6 Hopper JP'Jl"te§§!Uii"e-\-S S hnJH20 

On/Off 

No 1 Hopper OtJ 

No 2 Hoppel!" otJ 

No 3 Hopper OtJ 

No 4 Hopper ON 

No 5 Hopper ON 

No 6 Hopper btJ 

No 7 Hopper oJ 

No 8 Hoppe1r 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

_""_!_i.i. lililHzO 

-=_j__ hulHl.zO 

-.,:) h11HhO 

:::._._ 5 hnH20 

- , 5hniHh0 

Sc~rew 

Colfilveyol!" 

j 

j' 

/ 

/ v· 

/ 

./ 

,/' 

Nu 8 Hop pew Pre§silllre _ _.= ___ RlliiJHJ:zO 

No 9 JHoppew Pwess\lllr<e _.= _ _ll!11iH20 

No w IH!opper Presslt!lne -=--hlliHi 20 

No l -~ Hoppetr Pr<es§IUU"'<e -=-[!11iJHlz0 

Rotary Bag§ 

_ _::_I mdH[zO 

illlilf-!zO 

- hnlHI 20 

llllliH!zO 

Lock Chute Missing 

,/ / 0 

/ / 0 

/ J 0 

./ j 0 

/ 1/ () 

/ 1/ 0 

/ / 0 

EQUIPMENT PROBLEMS __________________________ _ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
-~--

--liME ---4 _flMP~ 

1:ss A.m, I fo l 

"'"":...;. 

10'-!D A,VV). __ Iss 

I"- • J5 ,v- A.~:,;.. I"\ 

::J: ~0 q,m. lb5 

!0 55 AM lb7 

\[ ·. \D A I frl,. I' I 

.~p~o 

JC, . -~.r A ·M I 6 d..-

~c A ,tv\, i ...... 

~9 I 

l'"_.., I ...., --' t. -tr\. ! i '-.. ....... _; I I:J-......i 

; ! • .-· 

i t:J:.: 

(' f 

~ \-:-:-- ~() 

3-15- J-013 

-~"t~K ___ 1~11P _ 

0 

37o. l_ ~ 

3l J_, \ 

0 

f 

L1 IS.to o_ 

r 

YY%.'6 0 

F 

o_ 

:3 ~~~ )_ t-

'-lOth~ 0 t 

7._ Qb I 

0 

f ...; .I ' fo 

~ )_( .l°F 

- - o. '-iYO.d.- t 

":"-, 

~~- ·-~· ;::_: ~ 

o'" •••-'Yo -••• 

,_ ·----~--.·-----.-

Di9.t'Y1ft{{ ft6lTLoN 

( Ql. -~-

/0?>.3 

l 03.3 

lO~. ~-

1~.7 ·-· 

I 

I OJ...1 

I 03, ~ I """ 

(D 3-~ 

(C? 3 ~ 

; !- 7 I . ~) _: • i 
[)attt: 

rime 

'.fempering Aiir Temp: 

-. '~ : . . 

''F Baghouse mower 

Inlet Tempemhure~ Tnu11sfer Blower: PSI 

Stack Tempe~ratmre: Air Pressan;re; ---~~~'- ___ PSI 

MAGNEHELIC GAUGES On Line Cleai!Ding On Line 

No 1 Hopper Pressvllne +5. S lnH20 =_L_htH20 No 7 Hopper Pressure + "7 lnHzO 

No 2 Hopper Pressure _±___$__ Inl]hO - .. S InH20 No 8 Hopper Pressure -=--InHzO 

No 3 Hopper Pressure i-S 5 InH20 -=l__ lnH20 No 9 Hopper Pressl!llre --=-lnHzO 

No 4 Hopper Pressure _±___5___InH20 -. 5 In.H20 No 10 Hopper Pressure--=-lnHzO 

No 5 Hopper Pressure ±_]_inH20 -45 InH20 No 11 Hopper P:ressi!llre-=-lnHzO 

No 6 Hopper Pressure __!_k_InH20 -=l_inH20 

Rotary Bags 

Cleaning -.- -- .. ~ lnHzO 

--=-lnHzO 

--~InH 0 

-=-lnH20 

-=-InHzO 

On/Off 

Screw 

Conveyor Lock Chute Missing 

No 1 Hopper OtJ " ./ / 0 

No 2 Hopper DtJ I ,J / 6 

No 3 Hopper QrJ J .,L j 0 

No 4 Hopper Qlll j / "- 0 

No SHopper otJ ./ ./ / 0 

No 6 Hopper abl ./ / 0 

No 7 Hopper otJ ;/ / ,,., 

No SHopper - No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

EQUIPMENT PROBLEMS. ________________________ _ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
Dat\l; 

T~m1:· 

-~4L.{".1 

--· _:.__ ~: 

Tempering Air Temp: 

l!!!Uet Temperah.H~re: 

Bagho!Ulst B!owei 

Translfe:r mow.er: 

.••• !., ____ _:_....:o........_ PSI 

PSI 

St!llck Temperahn·e: Air Pressure; _,:~ ____ PSI 

MAGNEHELIC GAUGES On Line Ciea~~ning On Li~~ne 

No l Hopper PressMre + S, S inH20 -:_L lnH20 No 7 Hopper Pressmre*:-· .. ::; lnHzO 

No 2 Hopper Pressure + S' lnH20 ~.s · InH20 No 8 Hopper Pressu11re _=:__InHzO 

No 3 Hopper Pressure ~s.s InH20 ..:::_LinH20 No 9 Hopper Pressure -=-lnHzO 

No 4 Hopper Pressure _:!:_k_InH20 -., S lnH20 NolO Hopper Pressure-=-InHzO 

No 5 Hopper Pressure _2]_ lnH20 -.5 InH20 No i 1 Hopper Pressure__:::____ lnHzO ( 

No 6 Hopper Pressl!llre ~ lnH20 -=-L InH20 

Rotary Bags 

Cleaning 

. -,..j- lnH20 

-=-lnH20 

-=-lnHzO 

__ lnH20 

-=-InfhO 

On/Off 

Screw 

Conveyor Lock Chute Missing 

No 1 Hopper OIJ J J / 0 

No 2 Hopper OrJ J / / 0 

No 3 Hopper 0~ ./ / / 0 

No 4 Hopper QN L / / 0 

No 5 Hopper o#J / / /' 0 

No 6 Hopper otJ 

No 7 Hopper QrJ 

/ / .t; 0 

/ >/ Q 

No 8 Hopper 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

EQUIPMENT PROBLEMS ________________________ _ 

MECHANICAL WORK PERFORMED. -------------------------------------------------

COMMENTS: 
I SJ 

I: 3o fvYl lbl tiOf:.l D 

F I 03.3 

I: 45 f n·i I to 1 L{L{). ?/'F i r Q{ -...t, ~ 

157 y bb .3 

0 

J.'00 f n" F 10~.3 

\ b s 133.\ 

0 

J~ tS fJi' .f l 03. ~ 

J ·. ~i) ft't), /66 45 b .l 0

f \ 0~. ~ 

~: '15 f y\\ J 6d.- Lf 3 ~.1 °f 1~.g 

(l 

~~Dtl f . "' t ~ \' \51 s 5~, 3 f l 0 3 ~3 

J b I . 0 

2> ·.IS r . 1\' I, Y.o~.~ F I o?>.j 

3:~o f,f() I~~ L( J-.ll 

0 

f I 03.) 

0 

.3:qs ~.r'). .. J(o5 ~ .JJ .7 F \0 ~. ~ 
3: 

.SnBo· ----- ... ·-···· 

---:-- """• (IF'} f'lllliij, U/2) ~2 ifijJJft~; (IF~} ~-m~"t~·· 

N21mt. __ .,) E FL ___ ~{_!_ii_( ? 0 -'f<.:.:!._ _____ _ 

Date: ______ 1_~-L~ __ :_~---~---------

Time :\ ; C.,... P. fYl --.--"-!~-------------------- ----

Tempering Air Temp: 0 JF lBaghmnse J!Uowew 

Tmnsfer lBDower: 

_ .. ~,_ _____ JP'SH 

Inlet Temperahnre: 0 JF PSH 

Stack Temperatu~re: 5 S '6 . d... oF Air Pwess1.11re: '0 ,._ PSI -~-

MAGNEHELIC GAUGES On Line Cleaning On Line 

No 1 Hopper Pressure __±_f_InH20 -=l_InH20 No 7 Hopper Pressun~ + l lnH20 

No 2 Hopper Pressure t5 InH20 - .S lnH20 No 8 Hopper Pressure --=--lnH20 

No 3 Hopper Pressure +5 lnH20 _::l_lnH20 No 9 Hopper Pressure -=-lnHzO 

No 4 Hopper Pressuret5. S' InHzO - 9 S" InH20 No 10 Hopper Pressure_:::_InHzO 

No 5 Hopper Pressure ~ lnH20 - .. 5 lnH20 No t 1 Hopper Pressure--=._ InHzO 

No 6 Hopper Pressure +- (c InH20 -=-l_InH20 

Screw Rotary Bags 

Cleaning 

. -. :.J InH20 

-=-InHzO 

_-_InH20 

_::_InHzO 

-=-InHzO 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper ON J ./ / 0 

No 2 Hopper otJ J ~ / C) 

No 3 Hopper ON ,/ J ./ C) 

No 4 Hopper ON J t/ / 0 

No 5 Hopper otJ ./ ../ / 

No 6 Hopper orJ ./ / / " 0 

No 7 Hopper orJ / / ,/ 0 

No 8 Hopper - - - No 9 Hopper - No 10 Hopper 

No 11 Hopper 

EQUWMENTPROBLEMS _________ ~-----------------------------

MECHANICAL WORK PERFORMED _________________________________ _ 

COMMENTS: 
,.-· ·- L,' i ........ ....._·' 1~-· f. 'fV', 

/'' < #~- .._i • . ..J • .._) 

) I I - ,- 1-)j ... i 

. 03. ._, -:z 

! / 1"'1"\ 

; bU 

' .- ? 

'0 :J f. ff\,' ; -... t ''-''0 

'0. 3D f.'(( \53 y b~ d.-oF I 03.3 

f. n\. 

() lo3 3 •:> ~-; 156 L..(t.fJ...S Fi6D Yl ~~ '1 

0 J '\ -. 

)() r.rn, t- o~._j 

l ·.IS f.M .. 15~ ~yo.3, 0 

"F J D~.~ 

0 

l: 30 f. (VI. I o33 \5\ . Ybi.Y f 
Tempeirll!!JJg Airr 

Ii!i~<et Tempewahnif'l2C~ 

Stack 1Lemperahnreo 

MAGNEHEUC GAUGES 

No 1 Hopper Pressl.ilre iS, S Jii!l!H20 

No 2 Hopper Pressmre + 5 ilfillH!20 

No.3 Hopper Pressure+ S. S inJHf 20 

No 4 Hopper Pressmne ~lnH 0 

No 5 Hopper Pressure ~ Inl-lhO 

No 6 Hopper JP'wessu!l"e ~lrrnH 0 

No 1 Hopper 

No 2 Hopper 

No 3 Hopper 

No 4 Hopper 

No 5 Hopper 

No 6 Hopper 

No 7 Hopper 

No 8 Hopper 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

On/Off 

Df.J 

OtJ 

(JtJ 

()tJ 

brJ 

ON 

otJ 

"F 

·ilik·· 

::F lFitniH. .' n: 

IB:a!gilno!llls~e Bllot-~N:r· 

'1fn.lflls1ferr Bno~·er: 

Oeal!llillllg On Lil!lle 

- 1 hnH20 No 7 Hopper P;ressllllir<e ·r -_;::_ hllll-ll 20 

- , ,j h11H20 No 8 Hopper Piress\Ulre ----=:__ h1HzO ! 

!nH20 No 9 Hopper PJressawe --=-~ imdH!zO 

- .. S lnHzO 

~InHzO 

-/ lllllthO 

Now Hoppe!r lP'ressll!l!re--=-hilH20 

No ! i Hoppe1r Pressure-=-ill1llHl 20 

Rotary Bags 

lP'Sli 

lP'SI 

,..... --· "') hnH2() 

-=-lllllH20 

----=--h1H20 

-=--JnH20 

-~lnH 0 

Screw 

Conveyor 

I 

Lock Chute Missing 

I 

/ 

_.L_ 

f 

j 

J 

/ 

/ 

1/ 

v/ 

,{ 

./ 

/ -0 

,/ .-:\ 

.J 

./ J 

/ .~"\ 

J 

J 0 

/ 0 

,j ~~ ,_; 

EQUWMENTPROBLEMS __________________________________________________ __ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
'. 

---4 4--- .' '' 

:! 

-~----1+- ··--------· --··----. ····-·· -·---------· -· .. ---------~-- <!!'··· i! . 

1_: oq_ ___ frr:. -l~- . _____ )b.~------ _ . ___ ~LS..1. ---------'-'------______ .. _________ ..!_P 3 :._L ____ .:... ___ . . 1; 

~ : 

·-·T'->--. --.,._,_,_, ___ <_"i1·-'·•o 'O' ·~•-' O"O·'<-----~-·---

;! ':""\.I~ .fj 

~-rs W'" 11 

.1~-~-----' -~------·+t· ; 

. 

~ ~ , __ tr_, ___ ---~----·-- -~--~----~ .. 

:r ~o PY>A ! l ; btL. -----·~~-----~:-t-··~---~----·~·--------· ---·'T•'-~ ·,•••' • 

ll 

----_;.;.,..;...~h- ' J 

1 l 

q ', Ll s f>\'Y"I_Jt---"-· •-Lb=D,;-_-- . lj . . -----!+········---- . -~------------ ><••• -----------~· --·-···------···· 

i l 

LQ~. OQ p~-- . u... --------'- Lb_S. ______ ....... -. 

11 

!J ---- ---~-------,___.,.. -~ -- « -- -'~'""' ----. -------~--~---- ~---------- --~---~-~-. ·•·•• ----~ -. 

j l . 10: JS pm . I l .. ----n---------------------------- -

--------·---··-···-·------

_..;.__..._.·-----·-----------------· ----····------·-

' d . --.-· ··-tt--~---------------· --------- ··• ---------------.----,···.------·-·- ---------------· ·-----------------· - ){) ~~() ,0 tv' ___ JJ. __________ -----------------······ -. ··• .. -···-. -·- ·- ··---~--··· ------··· . ., . .,.. 

······-···-·---------···-------"'-·--·-··------··-···-..... -----------····· 

ll . -----"'-- -it------ ----- -------·--· -·---------·-~---------------------------

' LOO PY'A it ____ _ ___ _ --J~------------------·---·- -~---- ____ :_ _____ , __________________________ _ 

U'.J.S P~ t1 .. H 
Jl . 

~--·- -~·~··''--

.3..:.J~~-~ _g-:-Ql3, 

_"Q':_gQ_ ELc 

Tempelri~rng Ai1r Temp: 

~lllllelt Tempemtulire: 

St21ck Temperature: 

\Fl\JMF [);~_: 

BaglhloruJse !Biow,eH 

TJrallllslfelf !Blower~ 

Air P res§llue: 

. 5 PSI 

PSI 

J.QcL__ PSI 

MAGNEHELIC GAUGES On Line Cleal!lling On Lim~ Cleanillllg 

-.,s InH20 

___::::._lnH20 

_:::-__ InH20 

No I Hopper Presswre+~lnH 0 .::J__InH20 No 7 Hopper Pressm:e~h:aH 0 

No 2 Hoppe1r Pressure -::_s_ lnH20 

No 3 Hopper Pressure -+-s. S InH20 

No 4 Hopper Pressmre~InH 0 

No 5 Hopper Pressure-+_-_; _lnH20 

No 6 Hopper Pressure LinH20 

On/Off 

No 1 Hopper ON 

No 2 Hopper ()_IJ 

No 3 Hopper 01\J 

No 4 Hopper QiJ 

No 5 Hopper ON 

No 6 Hopper ON 

No 7 Hopper DIJ 

No 8 Hopper 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

- l lnH20 

-~lnH 0 

-~InHzO 

- I InHzO 

Screw 

Conve:yor 

.,J 

J: 

I 

j 

J 

./ 

,z 

No 8 Hopper Pressure -=~Jnl-{zO 

No 9 Hoppe1r PresSII.lllre -=-lnH20 

No 10 Hoppe1r Pressure-=-InH20 

Noll Hopper Pressure-=---hnH20 

Rotary Bags 

-~~==: ... J nH20 

~Inf:hO 

Lock Chute Missing 

J j 0 

/ J 0 

/ J 0 

I / 0 

/ / C) 

/ ,j 0 

/ / 0 

EQUWMENT PROBLEMS. ________________________ _ 

MECHANICAL WORK PERFORMED ___________________ _ 

COMMENTS: 
Dat;e 

Tim,f· 

:~ ; j I 

-:~ r~'< _s.. _____ 13_:_~-.:_---~--::___._ --

S-Is- :::, 

("\ (.,C. 9h· 

-- --- ---·~-·-·---~·-

'; lj~(:> 

( LF vJ li !i, ,; :: /2:} 'l, 

Temperrillllg Aiw Temp: 

!llllh:\t Temperatillre: 

!B21gllnolVls<e Blowea 

Transferr JBnower: 

__ <c_? lP'Sll 

"lF lP'SK -·---------

Stack Temperatl!lnre: Air Pwessillnre: _ _j_Qp ____ lP'S n 

MAGNEHEUC GAUGES On Line Cleaning On Line 

No l Hopper lP'ress!Vlre ~InH 0 ~ i InH20 No 7 Hopper Pwess!lllre ~InHzO 

No 2 HopperlP'ressl!llr<e ~lnH 0 ~lnH 0 No 8 Hoppew Pwessure _!_IIllHzO 

No 3 Hopper Pressure + 5, 5 lnH20 -_!_lnH20 No 9 Hopper Pressure ) InHzO 

No 4 Hopper Pressure ! __ b __ _InH20 ~InH 0 No 10 Hopper Pressure { lnHzO 

No 5 Hopper Pressure ±..l_!nH10 ::_d_InH10 No II Hopper Pressure_\_InHzO 

No 6 Hoppew Pnessure !_Q__InH20 ~lnH 0 

Screw Rotary Bags 

Cleaning 

- ,5 lnH20 

1 lnH20 -~-

-t--InHzO 

I InH20 

rinH20 

On/Off Conveyor Lock Chute Missing 

No 1 Hopper ON -1 I .; Q 

No 2 Hopper orJ / -/ / 0 

No 3 Hopper ON / / v 0 

No 4 Hopper or) J ./ / a) 

No 5 Hopper alJ J / v (1 

No 6 Hopper o/11 -1 ./ j 0 

No 7 Hopper ol'f I j j 0 

No 8 Hopper ! i \ 

No 9 Hopper ! \ 

\ 

I ' 

No 10 Hopper =f I \ 

Noll Hopper I 

EQUIPMENT PROBLEMS ________________________ _ 

MECHANICAL WORK PERFORMED 

COMMENTS: 
N2!mC --- - _:_Jcr_:. ___ /..::.!cLSL•_ 

Dat~·; .:.- .::_. ;,D;}_, 

Time 

Tempedng Aiir Temp: 

Inlet Tempe~rahllre: 

Stack 1fempe;ahue; 

FUJM!lF D 

"IF 

~I 

--2. 

illrngilloaJJse mower 

Twa!lllsfe~r B!owe1r: 

Ailr JPressmre: 

JPSJI 

PSI --- --~----~-,.--

_ __jC!(! _PSI 

MAGNEHELIC GAUGES On Line Cleaning On Line Cleaning 

No l Hopper Pressure ~lnH 0 ~lnH 0 

No 2 Hopper Pres~nwre ~ lnH10 

No 3 Hopper Pressurel:_S__2__InH20 

No 4 Hopper Pressure-+_i _InH20 

No 5 Hopper Pressure~InH 0 

No 6 Hopper Pressuure"_t._lnH20 

On/Off 

No 1 Hopper 1\N 

No 2 Hopper atJ 

No 3 Hopper ()AI 

No 4 Hopper (,,.,/ 

No 5 Hopper """ 

No 6 Hopper ow 

No 7 Hopper r)l..! 

No 8 Hopper 

No 9 Hopper 

No 10 Hopper 

No 11 Hopper 

_l_lnHzO 

__.__L inHzO 

_)_lnHzO 

~lnHzO 

___;_j__ I nHz 0 

lnHzO 

Screw 

Conveyor 

/ 

/ 

-./ 

./ 

../ 

J 

./ 

I 

I 

I 

I 

No 7 Hoppe1r JP~ressure _ .. _7_1nH20 

No 8 Hoppeir Pnessmre ---+-.hllHzO 

No 9 Hopper P~ressure 1~ lnl:{zO 

No 10 Hopper Pressure lnHzO 

No ll Hopper Pressure lnHzO 

Rotary Bags 

· lnHzO 

InH20 

InH2 0 

_i_InH20 

Lock Chute Missing 

I a 

,; ../ 

,/ /') 

./ 1</ c 

./ ,/ c 

-/ / " 1\ 

--~ 

/ v (J 

I l 

I I 

I I 

I l 

EQUWMENTPROBLEMS _______________________________________________ __ 

J 

MECHANICAL WORK PERFORMED _____________________ _ 

COMMENTS: