# Exhaust Emissions Sampling Dal-Italia, Muskogee, OK Kiln Scrubber Exhaust May 3, 2006 Armstrong Environmental, Inc. Project W-2498-06

Report Prepared For: Bob Hurt Daltile 7834 C. F. Hawn Freeway Dallas, TX 75217

Report Prepared May 22, 2006 By: Arnzstrong Environmental, Inc. 7715 Sovereign Row Dallas, Texas 75247 (214) 631-0021

## TABLE OF CONTENTS Page

1. Yntroduction 1 H. Summary 2-3
III. Procedures 4-5 I'V. Appendices
A. Caiculation Summaries 6-8
B. Analytical Summaries 9- 14
C. Field Data Sheets 15 - l.8
D. Equipment Calibrations 19 - 25

# 1. INTRODUCTION

A series of tests was perfoizned on the exhaust associated with the Kiln Scrubber at the Dal-Italia facility in Muskogee, OK on May 3, 2006. The purpose of this test series was to deterrnine the exhaust einission rate of particulate in terms of lbslhr. Testing followed procedures detailed in Title 40: Code of FederaI Regulations (40:CFR). Sampling was perforrned by Richard Taylor, Gilbert Salinas and Tom Armstrong of Armstrong Environmental, Inc. using an Apex Method 5 sampling train. Three one hour test repetitions were perforrned according to the following schedule:

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## 5I3/06 8:25 AM .2:07 PM Submitted by:

## IL SUMMARY

A series of tests was performed on the exhatist associated with the Kiln Scnibber at the Dal-Italia facility in Muskogee, OK on May 3, 2006. Sampling was perfon-ned -followiiig procedures detailed -in Title 40: Code of Federal Regulations.
Results of this test series are summarized in Table 1. Results indicate the following particulate emission rates:

i"IX 

## A 5/3/06 Exhaust, lbs/hr 

## 3.371 3.470 2.905 3.249 

## Sampling was interrupted for approximately 95 

## minutes during Run #3 on 5/3/06.

2

### SUMMARY OF EMISSIONS TEST DATA
Table : 1 Plant : Dal-Italia, Muskogee, OK Location : Kiln Scrubber Exhaust Operator : R. Taylor Test Date : 3-May-06 Repetition : 1 2 3
STACK GAS Temperature, F 137.7 138.1 138.1 Velocity, fps 29.12 29.31 29.18 

### Volume Flow, acfm 33737.6 33958.9 33805.1

scfm 23899.3 24072.5 23989.6 scfh 1433955 1444349 1439374 Moisture, % 18.63% 18.52°' J o 18.43% CO2, % 2.50 2.50 3.00 02, % 18.00 18.00 18.00
SAMPLE Start Time, hrs:min 8:25 AM 9:55 AM 11:30 AM Finish Time, hrs:min 9:27 AM 10:27 AM 2:05 PM Sample Volume, scf 38.059 38.275 37.965 Isokinetic Ratio, % 101.5394 101.3814 100.9073
PARTICULATE

~ 

### _ ront Ha

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### l Samp e eight, mg 38.64 36.11 29.75 Concentration, gr/scf 0.015665 0.014557 0.012091 Emissions, Ibs/hr 3.210118 3.004605 2.487039
Back Half Sample Weight, mg 1.94 5.59 5.00 Concentration, gr/scf 0.000787 0.002253 0.002032 Emissions, Ibs/hr 0.161171 0.465127 0.41799 Total Particulate, Ibs/hr 3.371288 3.469732 2.905029

3

# III. PROCEDURES

The procedure for emissions sampling followed USEPA test methods as detailed in Title 40: Code of Federal Regulations. The following methods were used:
Method Title 1 Sample arnd Velocity Traverses for Stationary Sources
2 Determination of Stack Gas Velocity and Volumetric Flow Rate (Type S

Pitot Tube)
3 Gas Analysis for the Determination of Dry Molecular Weight
5 Determination of Particulate Emissions from Stationary Sources
202 Determination of Condensible Particulate Emissions from Stationary

Sources 02 and CO2 were determined using FyRite Analyzers. PM sampling was performed on the scrubber exhaust 

## for 3 minutes at each of 20 points, 10 points per traverse, making a total run duration of 60 minutes. A schematic of the sampling location is shown in Figure 1. The sampling train was configured as follows: Stainless Steel Sampling Nozzle Heated Glass Lined Probe Heated glass fiber filter Impinger #1 - 100 mis H20 Impinger #2 - 100 mis H20 Impinger 43 - 100 mis H20 Impinger #4 - Empty Impinger #5 - 200 grams silica Gel

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## Figure I- Kiln Scrubber Exhuast

Ln StcLl, Diemeter - 59.5 inclhes Roint #1 -1.S inci'iesPoint #2 - 4.9 incliesPoint #3 = 3.7 inches Point #4 - 13.4 inclies Point #S - 20.3 Inches f'oint #6 - 39.1 inches Poiilt #7 - 46.1 inches Point M3 - 50.6 in t, , hes Point #9 - 511.6 inclies Point #10 - -56 inchps

# Appendix A :EMISStON TEST SUMMARY

PLANT : Dal•Italia. Muskogee. 0K DATE : 3-May-06 PLACE : Kiln Scruhber Exhaiust RUN#: 1 TEST DURATION (MINUTES) : 60 LIQUID COLLECTED (mis) : 185.1 NOZZLE DiAMETER (INCH.) : 0.3043 PARTICULATE WEIGHT (Front hall rng) : 38.64 METER COEFFICIENT (Y) : 1 PARTICULATE WEIGHT (Back hali mg) : 1.94 PITOT COEFFICIENT (Cp) : 0.84 STATIC PRESSURE (En. H20) : •0.2 uAS METER VOL.(Cu.Ft.) : 39.8 PERCENT CO2 2.5 BAROMETRIC PRESSURE 29.5 PERCENT 02 18 PERCENT CO 0
FOR CIRCULAR STACK FOR RECTANGULAR STACK STACK DIAMETER (inch): 59.5 STACK LENGTH(inchs) : STACK AREA (Sq.Ft.) : 19.30907 STACK WIDTH(inchs) : NOZZLE AREA (leet): 0.000505 STACK AREA (Sq.FI.) : 0
ENTER THE STACK AREA SHOWN ABOVE: 19.30907 FLOWS SAMPLED VOLUME (STD. CU .FT.): 3B.0593 VOLUME OF WATER VAPOR (STD. CU .FT.): 8.7127 FRACTIONAL MOiSTURE CONTENT (QJ o ): 0.1863 DRY BASE: 79.5000 MOLECULAR WT. OF STACK GAS (DRY BASE): 29.1200 MOLECULAR WT. OF STACK GAS (WET BASE): 27.0486 STACK PRESSURE (inch Hg): 29.4853 STACK GAS VELOCITY (ft/sec.}: 29.1207 ACTUAL STACK GAS FLOW RATE (ACFM): 33737.6354 STANDARD STACK GAS FLOW RATE (SCFH): 1433955.26
PARTICULATE FRONT HALF PARTICULATE CONCENTRATION (GR./SCF): 0.0157 PARTICULATE CONCENTRATION (LBS/SCF): 2.24E-06 PARTICULATE EMISSION (LBS/HR): 3.2101

BACK HALF PARTICULATE CONCENTRATION (GR./SCF): 0,0008 PARTICULATE CONCENTRATION (LBS/SCF): 1.12E-07 PARTICULATE EMISSION (LBS/HR): 0.1612
ISOKINETIC RATIO (%): 101.5394

POINTS STACK T. DELTA P SQUAR D.P DELTA H METER T. METER T.

deg F INLET OUTLET

1 137 0.22 0.469042 1.10 77 77 2 138 0.20 0.447214 1.00 82 77 3 138 0.22 0.469042 1.10 84 78 4 138 0.22 0.469042 1.10 86 79 5 138 0.25 0.5 1.25 88 80 6 138 0.25 0.5 1.25 90 81 7 138 0.23 0.479583 1.20 92 81 8 138 0.23 0.479583 1.20 92 82

- 9 137 0.21 0.458258 1.10 92 82 10 137 0.15 0.387298 0.75 92 82 11 137 0.24 0.489898 1.20 85 83 12 138 0.25 0.5 1.30 92 84 13 137 0.26 0.509902 1.30 92 84 14 137 0.25 0.5 1.20 93 84 15 138 0.23 0.479583 1.10 92 84 16 138 0.22 0.469042 1.10 52 35 17 138 0.23 0.479583 1.10 91 85 18 138 0.21 0.458258 1,00 91 85 19 138 0.19 0.43589 0.94 90 85 20 138 0.15 0.387298 0.74 91 85

137.7 0.4684 1.1015 89.2000 82.1500 85.6750 

# REMISSION TEST SUMMARY

PLANT : aal•Italia. Masl<o;ee. OK DATE : 3-May-06 PLACE : Y.iln ScrubGer Exhaust RUN#: 2 TEST DURATION (MINUTES) : 60 LIQUID COLLECTED (mis) : 184.8 NOZZLE DIAMETER (INCH.) : 0.3043 PARTICULATE WEIGHT (Front half mg) : 36.11 METER COEFFICIENT (Y) : 1 PARTICULATE WEIGHT (Back half mg) : 5.59 PITOT COEFFICIENT (Cp) : 0.84 STATIC PRESSURE (in. H20) : •0.2 GAS METER VOL.(Cu.Ft.) : 39.989 PERCENT CO2 2.5 BAROMETRIC PRESSURE 29.5 PERCENT 02 18 PERCENT CO 0
FOR CIRCULAR STACK FOR RECTANGULAR STACK STACK DIAMETER (inch): 59.5 STACK LENGTH(inches) : STACK AREA (Sq.Ft.) : 19.30907 STACK WIDTH(inches) : NOZZLE AREA (teet): 0.000505 STACK AREA (Sq.Ft.) : 0
ENTER THE STACK AREA SHOWN ABOVE: 19.30907 FLOWS SAMPLED VOLUME (STD. CU .FT.): 38.2755 VOLUME OF WATER VAPOR (STD. CU .FT.): 8.6985 FRACTIONAL MOISTURE CONTENT (q o ): 0.1852 DRY BASE: 79.5000 MOLECULAR WT. OF STACK GAS (DRY BASE): 29.1200 MOLECULAR WT, OF STACK GAS (WET BASE): 27.0608 STACK PRESSURE (inch Hg): 29.4853 STACK GAS VELOCITY (ft/sec.): 29.3117 ACTUAL STACK GAS FLOW RATE (ACFM): 33958.9176 STANDARD STACK GAS FLOW RATE (SCFH): 1444348.7
PARTICULATE FRONT HALF PARTICULATE CONCENTRATION (GR./SCF): 0.0146 PARTICULATE CONCENTRATION (LBS/SCF): 2.08E-06 PARTICULATE EMISSION (LBS/HR): 3.0046
BACK HALF ~ PARTICULATE CONCENTRATION (GR./SCF): 0.0023 PARTICULATE CONCENTRATION (LBS/SCF): 3.22E•07 PARTICULATE EMISSION (LBS/HR): 0.4651 ISOKINETIC RATIO (%): 101.3814

POINTS STACK T. DELTA P SQUAR O.P DELTA H METER T. METER T.

deg F INLET OUTLET

1 138 0.19 0.43589 0.94 82 82 2 139 0.20 0.447214 0.99 84 82 3 138 0.23 0.479583 1.10 88 82 4 138 0.21 0.458258 1.00 86 82 5 138 0.23 0.479583 1.10 86 82 6 138 0.23 0.479583 1.10 87 82 7 138 0.22 0.469042 1.10 87 82 8 138 0.23 0.479583 1.10 88 82 9 138 0.23 0.479583 1.10 88 82 10 138 0.20 0.447214 0.99 88 82 11 13!9 0.24 0.489898 1.20 85 82 12 138 0.23 0.479583 1.10 90 83 13 138 0.25 0.5 1.20 90 83 14 138 0.26 0.509902 1.30 90 83 15 138 0.27 0.519615 1.30 90 83 16 138 0.24 0.489898 1.20 90 83 17 138 0.23 0.479583 1.10 90 83 18 138 0.22 0.469042 1,10 90 83 19 138 0.19 0.43589 0.94 89 83 20 133 0.16 0.4 0.79 89 83

138.1 0.4714 1.0875 87.8500 82.4500 85.1500

~''~EM1SSlON TEST SlJMMARY

PLANT 

# : ual•lialia. i'rSusisol;pe. Ott UATE 

# : 3•May•06 PLACE 

# : Y,itn Scrtihber Exhiust RUNi; 

# : 3 TEST DURATION (MINUTES) 

# : 60 LIQUID COLLECTED (m1s) 

# : 182.2 NOZZLE OIAMETER (INCH.) 

# : 0.3043 PARTICULATE WEIGHT (Front hall mg) 

# : 29.75 METER COEFFICIENT (Y) 

# : 1 PARTICULATE WEIGHT (Sack half mg) 

# : 5 PITOT COEFFICIENT (Cp) 

# : 0.84 STATIC PRESSURE (fn. H20) 

# : •0.21 GAS METER VOL.(Cu.Ft.) 

# : 40.03 PERCENT CO2 3 BAROMETRIC PRESSURE 29.5 PERCENT 02 18 PERCENT CO 

# . 0
FOR CIRCULAR STACK FOR RECTANGULAR STACK STACK DIAMETER (inch): 59.5 STACK LENGTH(inchs) 

# : STACK AREA (Sq.Ft.) 

# : 19.30907 STACK WIDTH(inchs) 

# : NOZZLE AREA (feet): 0.000505 STACK AREA (Sq.Ft.) 

# : 0
ENTER THE STACK AREA SHOWN ABOVE: 19.30907

FLOWS SAMPLED VOLUME (STD. CU .FT.): 37.9653 VOLUME OF WATER VAPOR (STD. CU .FT.): 8.5762 FRACTIONAL MOISTURE CONTENT 

### (°J o ): 0.1843 DRY BASE: 79.0000 MOLECULAR WT. OF STACK GAS (DRY BASE): 29.2000 MOLECULAR WT. OF STACK GAS (WET BASE): 27.1362 STACK PRESSURE (inch Hg): 29.4846 STACK GAS VELOCITY (ft/sec.): 29.1790 ACTUAL STACK GAS FLOW RA7E (ACFM): 33805.1152 STANDARD STACK GAS FLOW RATE (SCFH): 1439374.08
PARTICULATE FRONT HALF PARTICULATE CONCENTRATIOIV (GR./SCF): 0.0121 PARTICULATE CONCENTRATION (LBS/SCF): 1.73E•06 PARTICULATE EMISSION (LBS/HR): 2.4870
BACK HALF PARTICULATE CONCENTRATION (GR./SCF): 0.0020 PARTICULATE CONCENTRATION (LBS/SCF): 2.90F•07 PARTICULATE EMISSION (LBS/HR): 0.4180
1SOKINETIC RATIO (%): 100.9073

POINTS STACK T. DELTA P SQUAR D.P DELTA H METER T. METER T.

deg F 1NLET OUTLET

1 139 0.22 0.469042 1.10 83 83 2 

# ] 39 0.22 0.469042 1.10 86 84 3 138 0.22 0.469042 1.10 88 84 4 138 0.23 0.479583 1.10 90 85 5 138 0.24 0.489898 1.20 92 85 6 138 0.24 0.489898 1.20 93 86 7 138 0.22 0.469042 1.10 94 86 8 138 0.21 0.458258 1.00 94 87 9 138 0.20 0.447214 0.99 95 87 10 138 0:15 0.387298 0.75 89 88 11 138 0,26 0.509902 1.30 90 89 12 I38 0.26 0.509902 1.30 94 89 13 138 0.25 0.5 1.30 95 89 14 138 0.26 0.509902 1.30 95 89 15 138 0.26 0.509902 1.30 96 29 16 138 0.24 0.489898 1.20 96 90 17 138 0.21 0,458258 1.10 96 91 18 138 0.20 0.447214 1.00 96 91 19 138 0.19 0.43589 0.97 96 91 20 138 0.16 0.4 0.81 96 91

138.1 0.4700 1.1110 92.7000 87.7000 90.2000 

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### FILTER ANALITICAL DATA

Company: Dal-Italia, Muskogee, OK Date: 5/3106 Location: Kiln Scrubber Exhaust Run 1 Run 2 Run 3

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### 18.5 20.6 20.3



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## PARTICULATE ANALYTICAL DATA FORM
Company: Dal•Italia, Muskogee, 

### 0K Date: 

### 5/3/06 Location: Kiln Scrubber Exhaust Run 

### 1 Run 2 Run 

### 3 Density (Pa) Blank Concentration (Ca) Rinse Volume (Vaw) Residue in Rinse (Wa) 

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. 0.0004

Date of Weighing

Time Gross Weight Date of Weighing

Time 

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### 55, 89: io 4 

### - 11 1

Date of Weighing

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### 6,2 Date of Weighing 

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Time 

### j 2:..M Beaker Tare Weight 116.24-2 2, 2. 

### 9 5 Average Gross Weight 

### 95.0989 116.2479 101.3031 Less Blank Residue (Wa) 0.0004 0.0004 0.0004 Average Beaker Tare Weight 

### 95.0968 116.2422 

### 101.2998 Weight of Particulate in Rinse (mg) 

### 1.68 5.33 2.88



## H20 BLANK ANALYTICAL DATA FORM
Blank Volume (Va) Date of Weighing

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### v

Time Gross Weight Date of Weighing

Time Gross Weight Average Gross Weight 

### 98.22075 Date of Weighing

Time Tare Weight Date of Weighing

Time Tare Weight Average Tare Weight Weight of Blank (Ma) Ca= Ma/(Va"Pa) 

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# I COMMENTS:!APE Armslrong Environmental Inc. CONVERSION FACTORS EPA Method 5 522 Series Meter Box Calibralion 1 mm Hg : 0.13330 kPa Pre-Test Oririce Method 1 cm z 0.39370 lnch English Meter Box Units, English K Factor 1 mm = 0.03937 inch 1 cu ft a 28.32 lilers :ter Box i. 10 Dale: ----------- ------------- > 03/15/06 !rial tt: 30272 Baromelric Pressure: --- -- --- --> 29.95 (in. Hg) Theorelical Crilical Vacuum: --- > 14.13 (in. Hg)

Iill!

~ 1 0RTAN For valid tesl resuits, the Aclual Vacuum sliould be 1 to 2 In. Hg greaier lhan the Theoretica) Crilical Vacuum shown above. 'ORTAN The Critical Orifice Coefficienl. W. musl be entered in English units, (ft) 1, 3'(deg R)^0.5/((in.Hg)'(min)). !ili!

---------------- DRY GAS METER READINGS ---------------- -CRITICAL ORIFICE READINGS- -- Average Temperatures --

Vofunie Volume Volunie Initial Temps. Final Temps. Orifice K' Oritice Acluat -- Ambient Temperalure -- DGM DGM Anibient dH Tirzie Inilial Final Total Inlet Outlet Inlel Oullet Sarial# Coefficient Vacuum Initial Flnal Average Outlet Overall Temp H20) (r1iin) (cu tt) (cu (t) (cu it) (deg F) (deg F) (deg F) . (deg F) (number) (see above) (in Hg) (deg F) (deg F) (deg F) (deg R) (deg R) (deg R) 0.24 5.00 652.700 654.270 1.570 66.0 65.0 66.0 65.0 40 0.242 23.0 64.0 64.0 64.0 525.0 525.5 524.0 0.50 5.00 654.600 656.847 2.247 66.0 66.0 66.0 66.0 48 0.344 21.0 63.0 64.0 63.5 526.0 526.0 523.5 0.93 5.00 657.500 660.520 3.020 66.0 66.0 67.0 66.0 55 0.464 19.5 64.0 64.0 64.0 526.0 526.3 524.0 1.60 5.00 661.300 665.172 3.872 67.0 66.0 68.0 66,0 63 0.593 18.0 64.0 64.0 64.0 526.0 526.8 524.0 2.90 5.00 666.000 671.320 5.320 68.0 66.0 71.0 68.0 73 0.824 16.0 64.0 64.0 64.0 527.0 528.3 524.0

............................................... RESULTS ...................................................
)RY GAS METER --- --------- ORIFICE --------- -- DRY GAS METER -- --------- ORIFICE ------
.UME VOLUME ZRECT CORRECTED m(std) Vm(std) (cu il) (liters) 1.579 0.1 2.260 0.1 3.039 0.'1 3.899 0.2 5.359 0.2 VOLUME VOLUME VOLUME CORRECT CORRECT NOMINAL Vcr(sld) Vcr(std) Vcr (cu fl) (lilers) (cu fl) 1.585 0.1 1.572 2.253 0.1 2.233 3.035 0.1 3.010 3.882 0.2 ' 3.850 5.389 0.2 5.345 

### Ave ra g e Y ------- > CALIBRATION FACTOR Y Value Varialion (number) (number) 1.004 0.003 0.997 -0.003 0:999 -0.002 0.996 -0.005 1.006 0.006 

### 1.000 CALIBRATION FACTOR dH(g? Value Variation (in H20) (in H20) 1.352 -0.0635 1.391 -0.024 1.427 0.011 1.500 0.084 1.408 -0.008 

## 1.416 <------- Average dH@

: For Calibralion Faclor Y, the ralio of the reading of the calibration meter to the dry gas meter, rcceptabie tolerance of individual vaiues from ihe average is +-0.02.

- or Orifice Calibralion Faclor dH@, lhe orifice differential pressure in inches of H201hat equales to 0.75 cfm of air it 68 F and 29.92 inches_of Hg, acceptabie olerance of individual yaiues from the average is +-0.2.

SIGNED: 

### ~ / `-- ' 

### ~-" ti. ` ~J~_~ Date:

i...s

~

### Temperature Meter Calibrations

Meter Box #: 10, Date: 03l15106 

### Caiibrated By: RT

Emtech 42312 Degrees F Calibrator Probe Stack Oven Exit Auxillary
Point 1 32 33 32 34 32 32
Point 2 212 213 212 214 212 212
Point 3 752 754 752 754 752 752

Emtech 42312 Degrees R Calibrator Probe Stack Oven Exit Auxillary
Point 1 492 ' 

### 493 492 494 492 492
Point 2 672 673 672 674 672 672
Point 3 1212 1214 1212 1214 1212 1212

Percent Difference Probe Stack Oven Exit Auxiliary
Point 1 0.20284 0 0.404858 0 0
Point 2 0.148588 0 0.296736 0 0
Point 3 0.164745 0 0.164745 0 0



# 2-0CALIBRATION FACTOR dH a rD Value Variation (in H20) (in H20) 1.416 0.0013 1.413 -0.001 1.415 -0.000 

## 1.415 <------- Average dH@ Armstrong Environmental Inc. CONVERSION FACTORS

EPA Method 5 511 Series Meter Box Calibration 1 mm Hg = 0,13330 kPa Post-Test Orifice Method 1 cm = 0.39370 inch English Meter Box Units, English K' Factor 1 mm = 0.03937 inch 1 cu ft= 28.32 liters er Box 4 10 Date: -----------------------> 05/04106 ial #: 30272 Barometric Pressure: •----••---> 29.70 (in. Hg) Theoretical Critical Vacuum: --- > 14.01 (in. Hg)
!!! 'ORTAt\ For valid test results, the Actual Vacuum shouid be 1 to 2 in. Hg greater than the Theoretical Critical Vacuum shovan above. 'ORTAI\ The Critical Orifice Coefficient, K, must be entered In English units, (ft)"3'(deg R)"0.5/((in.Hg)`(min)). H!

------ --------- DRY GAS METER READINGS --------=------- -CRITICAL ORIFICE READINGSTheoretical Critical Vacuum:---> 14.01 (in. Hg) Volume Volume Volume Initial Temps. Final Temps. Orifice K' Orifice Actual - Ambient Temperature - DGM DGM Ambient dH Time Initial Final Total Inlet Outlet Inlet Outlet Serial#t Coefficient Vacuum Initial Final Average Outlet Overall Temp 120) (min) (cu ft) (cu ft) (cu ft) (deg F) (deg F) (deg F) (deg F) (number) (see above) (in Hg) (deg F) (deg F) (deg F) (deg R) (deg R) (deg R) 0.91 10.00 435.400 441.533 6.133 75.0 74.0 77.0 76.0 55 0.464 19.5 75.0 77.0 76.0 535.0 535.5 536.0 0.91 5.00 441.900 444.972 3.072 77.0 77.0 78.0 77.0 55 0.464 19.5 77.0 77.0 77.0 537.0 537.3 537.0 0.91 5.00 445.200 448.268 3.068 78.0 77.0 79.0 78.0 55 0.464 19.5 78.0 78.0 78.0 537.5 538.0 538.0

0/4110//t//.f/f////////.//////,/*/f/fR///1////// RESULTS ///A////1//.//.//////////q11///!i//.11/ff/./f►l11.ffR•
RY GAS METER --- ----- --- ORIFICE ----•---- - DRY GAS METER - -- ORIFICE
UME VOLUME VOLUME VOLUME VOLUME CALIBRATION FACTOR :RECTI CORRECTED CORRECTI CORRECTI NOMINAL Y m(std) Vm(std) Vcr(std) Vcr(std) Vcr Value Variation (cu ft) (liters) (cu ft) (iiters) (cu ft) (number) (number) 6.014 0.2 5.951 0.2 6.088 0.990 -0.001 3.002 0.1 2.973 0.1 3.047 0.990 -0.000 2.994 0.1 2.970 0.1 3.050 0.992 0.001 

## Average Y -------> 0.991

For Calibration Factor Y, the ratio of the reading of the calibration meter to the dry gas meter, icceptable tolerance of individual vaiues from the average is +-0.02. =or Orifice Calibration Factor dH@, the orifice differential pressure in inches of H20 that equates to 0.75 cfm of air it 68 F and 29.92 inches of Hg, acce table lerance of , in ' idual values from the average is +-0.2.
SIGNED: 

## ~ Date:



# r'

~ "°'t

### Temperature Mefier Cafibrations

Meter Box #: 10 Date: 05/04I06 

### Catibrated By: RT

Emtech 42312 Degrees F Calibrator Probe Stack Oven Exit Auxiliary
Point 1 68 69 68 68 67 68
Point 2 138 139 138 139 138 138
Point 3 250 252 250 251 250 250

Emtech 42312 

### Degrees R Calibrator Probe Stack Oven Exit Auxillary
Point 1 528 529 528 528 527 528
Point 2 598 599 598 599 598 598
Point 3 710 712 710 711 710 710

Percent Difference Probe Stack Oven Exit Auxiliary
Point 1 0,189036 0 0 0.189394 0
Point 2 0.166945 0 0.166945 0 0
Point 3 0.280899 0 0.140647 0 0

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