### SOURCE OWNER: 

## Dal Italia

**PLA NT LOCA** 

**TION:** 

## Muskogee, Oklahoma **SOURCE(S) NA ME(S):**  

## We t Scrubber 2 **SOURCE(S) CONDITION:** 

## Normal Conditions-Tile MACT **SOURCE(S) SHA PE:**  

## Circular **TEST PERFORMED:** 

## Flow and FTIR **REFERENCE METHOD TESTS:** 

## Sample Test Points at Location EPA Method 1 Volumetric Flow

and Gas Velocity EPA Method 2 Molecular W eight EPA Method 3 / 3A Moisture Content EPA Method 4 Hydrogen Chloride EPA Method 320 Hydrogen Fluoride EPA Method 320 **ENTEC PROJECT MA NA** **GER (PM)** 

## Lynn Beane **ENVIRONMENTA L A** **NA LYST (Team Leader)**  

## Erik Groth **ENVIRONMENTA L A** **NA LYST (A**  **ssistants)** 

## John Drienzo **OWNER'S REPRESENTA TIVE(s):**  

## Mr. Bob Hurt and Mr. Steve W illis **ENTEC PROJECT NUMBER:** 

## 210155 **DA TES TESTS CONDUCTED:**  

## Trav/Prep Run 1 Run 2 Run 3 05/13/10 05/14/10 05/14/10 05/14/10 Thursday Friday Friday Friday

4 5 5 5 

# Entec Services, Inc. **SOURCE OVERVIEW**

### Client: **Dal Italia** Job No. : Source: **Wet Scrubber 2** Input By:
**V Port Type**  **Nipple Port Diameter**  **72 50.0**  **Inches**

**80.0 1.11**  **144.0 2.00**  **8 8** 

x' to Force More Points? **Point No. 1**  **2.3 17.3**  **2 7.6**  **22.6 3**  **14.0 29.0**  **4 23.3**  **38.3 5**  **48.7 63.7**  **6 58.0**  **73.0 7**  **64.4 79.4**  **8 69.7**  **84.7**

*** Adjusted points diameter > 24" no point closer than 1.0 inch** *** Adjusted points diameter <** **24" no point closer than 0.5 inch Stack Diameters between 12-24 inches minimum points are 8 ;**  **4 points per port if the 8 / 2 diameters downstream and upstream criteria is met.** 



### QC'd by: JRF **'Before' Flow Disturbance, Distance (B):**

**Inches**

**INCHES** 

## 72.0 **INCHES**

**INCHES**



## 144.0 **80.0** 

# Figure 4-1 **Entec Services, Inc** 16 D Commerce Ave. Hueytown, AL 35023 

## STA **CK DRA WING & TRA** 

**VERSE POINT LOCA**

**TI ON** 

**28.274 Stack Area, Ft** 

**2 :**  

### 210155 **Erik Groth**
**4**
**Stack Height, feet: 15.00** 

**Inches 16**  **Total Number of Traverse Points: Number of Points per port / traverse:** 

**Inside Stack Outside Nipple**  **'After' Flow Disturbance, Distance (A): Stack Diameter, inches:** 

**Stack Properties: Type of Traverse: Velocity (V) or Particulate (P):** 

**Number of Ports: Length of Port, inches:**  **2**

### Client: **Source:** 

### Traverse Point **Delta P Sq. Rt. Delta P**  **Stack Temp. (°F)** 1-1 0.0000 1-2 0.0000 1-3 0.0000 1-4 0.0000 1-5 0.0000 1-6 0.0000 1-7 0.0000 1-8 0.0000 2-1 0.0000 2-2 0.0000 2-3 0.0000 2-4 0.0000 2-5 0.0000 2-6 0.0000 2-7 0.0000 2-8 0.0000



### Average **#DIV/0! 0.0000**  **#DIV/0! QC'd by: JRF**  

### Note: Micro-monometer required based on preliminary **low flows. Note: The cy** 

**clonic flows were not tested based on the absence of cy clonic flow from previous test results.** 



### Null Reading (Angle) **Preliminary**

**Traverse & Cy**

**clonic Flow Verification** 

# ENTEC Services, Inc.

**Test Date: Run No.:**  **05/13/10 Preliminary Test**  **Dal Italia** 16 D Commerce Ave, Hueytown, AL 35023



### Wet Scrubber 2

### Dal Italia
**We t Scrubber 2** 


### 1.986
**0.987**

**Deg. R 547.0** 


# Y**o** 

# = **1.005 10 / (Volume)**  **X** **SQRT ((0.0319 * (Tm/Pbar))** 

## 1.303 **X** 

## 0.772 QC'd by: JRF



## Date: **88.0 Source:**  **Job Number:**

**Original Y Factor: 210155** 

**87.0 Calibration Date:**  **9/29/2009**

**Initial Volume: 87.200**  **Final Meter Temperature: Final Volume:**  **94.875 Initial Meter Temperature:** 

**Av erage Temperature:** 



## Y**o**

## Equation: **29.30 Barometric Pressure:** 



## Signature: 

# Meter Calibration %**Difference = -1.87%**  **86.0**
**Meter Volume:**



## Y**o**

## Result: **7.675** 

# ENTEC Services, Inc. 16-D Commerce Ave. Hueytown, Alabama 35023


# Initial Meter Box 10 Minute Calibration

**Meter Box: Original Delta H @:**  **NC-2 Client:**  **Location: Muskogee, Oklahoma** **Test Run Preliminary**  Meter Temperature **(estimated based on elevated ambient) 100**  Stack Temperature **( Preliminary Traverse Average**  **) #DIV/0!**  Pitot Tube Correction Factor **(calibration or 0.84** **for S-Type and 0.99** **for Standard pitot) 0.840**  Delta H@ **(Identified on Meter Box) 1.986**  Meter Correction Factor **(Identified on Meter Box) 0.987**  Molecular W eight of Dry Air **29.400** Average Delta H Desired 2 Average Delta P **( Preliminary Traverse Average**  **) #DIV/0!**  Percent O2 **(Estimate / Preliminary Measurement) 7.00**  Percent CO2 **(Estimate / Preliminary Measurement) 7.00**  Barometric Pressure **(Calibrated Barometer) 29.99**  Static Pressure at Stack, in. w .g. **(Remove +/- Pitot) 0.20** 
Percent Moisture @ Saturation **(if scrubber is saturated) #DIV/0!**  % Moisture in Stack Gas **(Estimate / Preliminary Meth. 4/ Saturation) 7.00**  Suggested Nozzle Diameter/Calculated - **Normal #DIV/0!**  **Nozzle Selected 0.2500**  **Total Test Time, Minutes 60.0**  **Required Meter Volume (from industry subpart) 120.0**  Calculated Nozzle to Meet Required Volume from subpart **#DIV/0!** Estimated Meter Volume for each Test Run #DIV/0! **High Delta P ( Based on Preliminary Readings**  **) Keep below highest cal point**  **0.00 Low Delta P (**  **Based on Preliminary Readings )**  **0.00** Meter Pressure @ high Delta P #DIV/0! Meter Pressure @ low

Delta P #DIV/0! **K-Factor #DIV/0!**  Calculated or linked Data (locked) **Black** Linked Data that can be changed (unlocked) **Red** Data that needs input values (unlocked) **Blue**

Molecular weight of Dry Air ( **30.00** ) **Hidden**

Average Delta H ( **1.00** ) **Hidden** Orifice Flow

Rate ( **0.75** ) **Hidden** Moisture Fraction @ Meter ( **0.00** ) **Hidden** Molecular W eight @ Meter ( **29.00** ) **Hidden** Absolute Pressure @ Meter (calculated from preliminary traverse and input data) **Hidden** Absolute Pressure @ Stack (calculated from preliminary traverse and input data) **Hidden**

Velocity, FPS (calculated from preliminary traverse and input data) **Hidden** ACFM (calculated from preliminary traverse and input data) **Hidden** DSCFM (calculated from preliminary traverse and input data) **Hidden**



## Input Data

**Calculated Data** 

# Entec Serv **ices, Inc.** K Factor Determination

# FTIR Raw Input **Results Summary (from FTIR Output)** See Raw Results from FTIR Data Set 

## Time (24-hr) Measured Concentration, ppm (wet, v/v) Run Date Start Run End Run Hydrogen Chloride HCl Hydrogen Fluoride

HF 1 05/14/10 14:03:00 15:04:00 7.88 8.94 2 05/14/10 15:27:00 16:30:00 12.63 10.55 3 05/14/10 16:55:00 17:58:00 4.98 5.65

### Client:

Source: **Wet Scrubber 2** 

### Symbol **Units Test Data**  QC'd by: JRF

**- -**  **1 2**  **3 AVERAGE**  

### Test Date **- -**  

### 05/14/10 05/14/10 05/14/10 05/14/10 All Runs Times, Pollutant Runs (Began - Ended) **- Military Time**  

### 1403-1504 1527-1630 1655-1758
- Times, Flow Runs (Began - Ended) **- Military Time**  

### 1403-1504 1527-1630 1655-1758 1800-1814 Sampling Time  **minutes** 

### 60.0 60.0 60.0
- 60.0 Stack Area **A s**  **Ft 2**  

### 28.27 28.27 28.27 28.27
- Barometric Pressure **P bar**  **in. Hg** 

### 29.79 30.01 30.01 30.01 29.96 Stack Static Pressure **P g**  **in. H 2**  **0** 

### 0.37 0.45 0.45 0.45 0.43 Oxygen Concentration, % (dry basis) **O 2**  **%** 

### 19.0 19.0 19.0 19.0 19.00 Carbon Dioxide Concentration, % (dry basis) **CO 2**  **%** 

### 2.0 2.0 2.0 2.0 2.00 Avg. Sq. Rt. of Delta P **sqrt**  **P (in. H20)1 / 2**  

### 0.702 0.702 0.702 0.702 0.702 Stack Temperature **t s**  **o F**  

### 133.5 133.5 133.5 133.5 133.5 Hydrogen Chloride (FTIR), ppm, wet **HCl ppm, wet**  

### 7.884 12.634 4.976 8.498 Hydrogen Fluoride (FTIR), ppm, wet **HF ppm, wet**  

### 8.944 10.555 5.651 8.383 Hydrogen Chloride (FTIR), ppm, dry **HCl ppm, d, v / v**  

### 9.400 15.103 5.965 10.156 Hydrogen Fluoride (FTIR), ppm, dry **HF ppm, d, v / v**  

### 10.664 12.618 6.773 10.018 Run Number 

### Field Data Data Input By: **210155 Lynn Beane**  Job No.: **Dal Italia** 

# ENTEC Serv**ices, Inc.** 16-D Commerce Ave. Hueytown, Alabama 35023 

## INPUT TEST DATAClient:

Source: **Wet Scrubber 2 Formulas**  **Symbol Units**  **Calculated Data** QC'd by: JRF Run Numbers

- - **1 2**  **3 4**  **AVERAGE** Test Date(s)

- - 05/14/10 05/14/10 05/14/10 05/14/10 3 Runs Times, Pollutant Runs (Began - Ended)

- Military Time 1403-1504 1527-1630 1655-1758 0
- Times, Flow Runs (Began - Ended)

- Military Time 1403-1504 1527-1630 1655-1758 1800-1815 1. Stack Pressure **= P bar**  **+ P g**  **/ 13.6** P s in. Hg 29.82 30.04 30.04 30.04 29.97 2. Meter Pressure **= P bar**  **+**  **H / 13.6** P m in. Hg 29.79 30.01 30.01 29.94 3. Standard Meter Volume **= 17.64* Y* (V** **m /T**  **m** **)* (P** **bar +**   **H / 13.6)** V m(std) dscf 0.000 0.000 0.000 0.00 4a. Standard Volume of W ater Vapor Condensed **=0.04706*W****imp** Vwc(std) scf 0.000 0.000 0.000 0.00 4b. Standard Volume of W ater Collected in Silica Gel **=0.04715*W****sg** Vwsg(std) scf 0.000 0.000 0.000 0.00 5. Moisture Fraction **=(V wc(std)**  **+ V wsg(std)** **)/(V wc(std)** **+ V wsg(std)** **+ V m(std)** **)** B ws fraction 0.1613 0.1635 0.1657 0.1635 0.16 9. Molecular W eight of Stack Gas (dry basis) **= 0.32*(O** **2****)+ 0.44*(CO** **2****)+0.28*(100-(O** **2 )-(CO**  **2 ))**  M d g / g-mole 29.144 29.080 28.992 29.072 29.07 10. Molecular W eight of Stack Gas (wet basis) **= M d** ***(1-B ws** **)+18.0*(B** **ws )**  M s g / g-mole 27.347 27.268 27.171 27.262 27.26 11. Average Stack Gas Velocity **= 85.49*C** **p*****(sqrt**  **P) avg** ***SQRT((T s** **) / (P s** ***M w** **))** v s ft / s 42.89 42.89 42.89 42.89 42.89 12. Stack Gas Flow @ Actual Conditions **= 60*v****s*****A s**  Q a acfm 72,766 72,766 72,766 72,766 72766 13. Stack Gas Flow @ STP **= Q a** ***(T std** **/T s** **)*(P** **s /P**  **std )**  Q s scfm 64,971 64,971 64,971 64,971 64971 14. Stack Gas Flow @ STP, dry **= Q a** ***(1-B ws** **)*(T** **std /T**  **s****)*(P** **s /P**  **std )**  Q std dscfm 54,349 54,349 54,349 54,349 54349 15. Hydrogen Chloride Conc. @ Std.Conditions **=(0.01543*HCl** **mg )/V** **m(std)** HCl cs gr / dscf 0.00621 0.00998 0.00394
- 0.01 15. Hydrogen Fluoride Conc. @ Std.Conditions **=(0.01543*HF** **mg )/V** **m(std)** HFcs gr / dscf 0.00387 0.00458 0.00246
- 0.00 21. Hydrogen Chloride Mass Emissions **=(60/7000)*HClcs*Q** **std** HCl lbs/ hr lbs / hr 2.89 4.65 1.84
- 3.13 32. Hydrogen Fluoride Mass Emissions **=(60/7000)*HFcs*Q** **std** HF -lbs / hr lbs / hr 1.80 2.13 1.14
- 1.69 

### CA**LCULA**

**TED TEST DA**

**TA - Metric Units**  **Formulas** Symbol Units **Calculated Data** QC'd by: JRF Run Number

- - **1 2**  **3 4**  **AVERAGE** Test Date

- - 05/14/10 05/14/10 05/14/10 05/14/10 3 Runs Times, Pollutant Runs (Began - Ended)

- Military Time 1403-1504 1527-1630 1655-1758
- - 1. Stack Pressure **= P s** ***25.4** P s mm. Hg 757.36 763.09 763.09 763.09 761.66 5. Moisture Fraction **=(V wc(std)**  **+ V wsg(std)** **)/(V wc(std)** **+ V wsg(std)** **+ V m(std)** **)** B ws fraction 0.161 0.163 0.166 0.163 0.163 9. Molecular W eight of Stack Gas, dry basis **= 0.32*(O** **2****)+ 0.44*(CO** **2****)+0.28*(100-(O** **2 )-(CO**  **2 ))**  M d g / g-mole 29.144 29.080 28.992 29.072 29.072 10. Molecular W eight of Stack Gas, wet basis **= M d** ***(1-B ws** **)+18.0*(B** **ws )**  M s g / g-mole 27.347 27.268 27.171 27.262 27.262 11. Average Stack Gas Velocity **= 85.49*C** **p*****(sqrt**  **P) avg** ***SQRT((T s** **) / (P s** ***M w** **))** v s m / s 13.07 13.07 13.07 13.07 13.07 12. Stack Gas Flow @ Actual Conditions **= 60*v****s*****A s**  Q a acmm 2,061 2,061 2,061 2,061 2,061 13. Stack Gas Flow @ STP **= Q a** ***(T std** **/T s** **)*(P** **s /P**  **std )**  Q s scmm 1,840 1,840 1,840 1,840 1,840 14. Stack Gas Flow @ STP (dry) **= Q a** ***(1-B ws** **)*(T** **std /T**  **s****)*(P** **s /P**  **std )**  Q std, d dscmm 1,539 1,539 1,539 1,539 1,539 15. Hydrogen Chloride Conc. @ Std.Conditions ( FTIR) **=(0.01543*HCl** **mg )/V** **m(std)** HCl cs mg / dscm 14.217 22.841 9.021
- 15.360 15. Hydrogen Fluoride Conc. @ Std.Conditions (FTIR) **=(0.01543*HF** **mg )/V** **m(std)** HFcs mg / dscm 8.851 10.473 5.622
- 8.3154 15. Hydrogen Chloride Conc @ 7% O2 **=C s**  *** ((20.9-7)/(20.9-% O2))**  c %O2 mg / dscm c 85.92 167.10 59.71
- 104.24 15. Hydrogen Fluoride Conc @ 7% O2 **=C s**  *** ((20.9-7)/(20.9-% O2))**  c %O2 mg / dscm c 53.49 76.62 37.21
- 55.77 21. Hydrogen Chloride Mass Emissions **=(60/7000)*HClcs*Q** **std** HCl kg / hr kg / hr 1.3128 2.1091 0.8330
- 1.4183 21. Hydrogen Fluoride Mass Emissions **=(60/7000)*HFcs*Q** **std** HCl kg / hr kg / hr 0.8173 0.9671 0.5191
- 0.7678 **Description**

**Description Dal Italia**  Job No.: **210155** Data Input By: **Lynn Beane** 

# ENTEC Serv**ices, Inc.** 16-D Commerce Ave. Hueytown, Alabama 35023 

### CA**LCULA**

**TED TEST DA**

**TA - English Units** 

# Emissions Summary

**Test Performed For: Testing Performed By:**  **Muskogee, Oklahoma Birmingham Division**  **Source(s) Tested: Wet Scrubber 2**  **Project Manager: Test Condition:**  **Normal Conditions-Tile MACT Lynn Beane**  **Test(s) Performed:**

**Run Number 1**  **2 3**  **4 Av** **erage** 

### Date of Run 5/14/10 5/14/10 5/14/10 5/14/10 **3 Runs** 

### Times, Pollutant Runs (Began - Ended) 1403-1504 1527-1630 1655-1758
- - 

### Times, Flow Runs (Began - Ended) 1403-1504 1527-1630 1655-1758 1800-1814
- 

### Oxygen Conc., % (dry basis) 19.0 19.0 19.0 19.0 19.0 

### Carbon Dioxide Conc. % (dry basis) 2.0 2.0 2.0 2.0 2.0 

### Molecular W eight Of Stack Gas % (dry basis) 29.08 29.08 29.08 29.08 29.07 

### Molecular W eight Of Stack Gas % (wet basis) 27.27 27.27 27.27 27.27 27.26 

### Hydrogen Chloride ppm, v / v, d 9.40 15.10 5.96
- 10.16 

### Hydrogen Fluoride ppm, v / v, d 10.66 12.62 6.77
- 10.02 

### Stack Temperature o C 56.4 56.4 56.4 56.4 56.4 

### Moisture Content %, v / v 16.13 16.35 16.57 16.35 16.35 

### Average Stack Gas Velocity m / s 13.07 13.07 13.07 13.07 13.07 

### Stack Gas Flow @ Actual Conditions acmm 2,061 2,061 2,061 2,061 2061 

### Stack Gas Flow @ STP scmm 1,840 1,840 1,840 1,840 1840 

### Stack Gas Flow @ Dry Standard Conditions dscmm 1,539 1,539 1,539 1,539 1539 **Hydrogen Chloride Conc. @ STP** 

### mg / dscm **14.22 22.84**  **9.02 -**  **15.36 Hydrogen Fluoride Conc. @ STP**  

### mg / dscm **8.85 10.47**  **5.62 -**  **8.32 Hydrogen Chloride Conc @ 7%**  **O2** 

### mg / dscm c 

### 85.92 **167.10 59.71**  **- 104.24**  **Hydrogen Fluoride Conc @ 7% O2**  

### mg / dscm c 

### 53.49 **76.62 37.21**  **- 55.77**  **Hydrogen Chloride Mass Emissions** 

### kg / hr **1.313 2.109**  **0.833 -**  **1.418 Hydrogen Fluoride Mass Emissions**  

### kg / hr **0.817 0.967**  **0.519 -**  **0.768**  Flow testing was performed for this source in conjunction with the Method 29 Testing, Run 2.**  

### Dal Italia

**Flows, Moistures, HCl and HF**

[NOTE - Run 4 Flow was completed as a Post-ICR flow run to bracket the 3 ICR runs.] 

# Table 2-6

# Note: This page shall only **be amended by**

**Tommy Lotz, Jr. or Tom Lotz, Sr.**  **The use of this page is to track amendments to the templates and to verify most current versions. Ad**  **ditionally this page will provide information to Project Leaders, Project Managers, Report Writers, and QA /QC Officers to ensure data accuracy**  

# Note: Project leaders and Project Mangers please check these items before posting file to server 1 2 3 4 5 Make sure that all unknown inputs are highlighted in yellow 6 Attempt to reduce the amount of yellow/unknowns before turning data in for report writing 7 Review the data to make sure that nothing seems out of whack i.e. one run gravely different from another (use calculations page) 8 Make sure that the correct lines on the calculation page are hidden/unhidden ask if unsure 9 Check saturation (theoretical) equations to make sure that they are only revealed when testing on ambient or scrubber sources 10 Make sure that you note any problems with the testing in relationship to this spreadsheet to the report writer in writing (email OK) 11 **If AN**  **Y amendments to the spreadsheet are made make sure that y** **ou notify the report w**  **riter in w riting (email OK)**  12 Make sure that the stack dimensions page is accurate and completed 13 Make sure that the correct name of the page input person is on each page 14 15 FTIR Operators see note #43 on Tracking Page tab (to get started)

DoList 11 June 010

Compare Fo to look up table (pass/fail ) diluents Inputs sheet for ppm from RataMAtion link Autom ate rund dates Add 027 Lab Add 2F Sheet for 3D Probe Autom ate test methods Clean up and expand metrics, inc temp and pressure 

# Note: This page shall nev**er be deleted under any circumstances**

Delete unused pages i.e. Square, Run 4, Deionized H2O, or 202 lab when not used in testing. Remove unnecessary pages - if unsure ask 

# Template Checks This template is reduced to it's simplest form. All additional lines are hidden. Unhide them as needed. Method and Testing groups that are hidden are color coded for reference. They are loosely grouped together. Make sure all data is correctly and completely input on all pages

# Note: This page shall only **be amended by**

**Tommy Lotz, Jr. or Tom Lotz, Sr.**  **The use of this page is to track amendments to the templates and to verify most current versions. Ad**  **ditionally this page will provide information to Project Leaders, Project Managers, Report Writers, and QA /QC Officers to ensure data accuracy**  

# Note: Project leaders and Project Mangers please check these items before posting file to server

Attempt to reduce the amount of yellow/unknowns before turning data in for report writing Review the data to make sure that nothing seems out of whack i.e. one run gravely different from another (use calculations page) Make sure that the correct lines on the calculation page are hidden/unhidden ask if unsure Check saturation (theoretical) equations to make sure that they are only revealed when testing on ambient or scrubber sources Make sure that you note any problems with the testing in relationship to this spreadsheet to the report writer in writing (email OK) **amendments to the spreadsheet are made make sure that y ou notify**  **the report w riter in w**  **riting (email OK)** 

# Note: This page shall nev**er be deleted under any circumstances**

Delete unused pages i.e. Square, Run 4, Deionized H2O, or 202 lab when not used in testing. This template is reduced to it's simplest form. All additional lines are hidden. Unhide them as needed. Method and Testing groups that are hidden are color coded for reference. They are loosely grouped together.

## Mi

**ller #2 Flue Dimensions (inches)** History (r3, JF, 26 Apr 010) 

## Absorber Stack Inlet Outlet Paltform Tests Methods 3A,/6C, 2/4/5B, Size 3A, 6C 3A (bag), 2/4/5B Stack Height Feet n/a n/a 700 Wo rking height Feet < 75 ~ 175 463

Access Stairs Stairs/Elevator?? Elevator Flue Shape Rectangle Round Round

Flow Direction Lateral Lateral Vertical Ports Diameter 4.0 4.0 4.0

Type NPT (cap) Flange Flange Length (23.5 varies) 41.5 12.0 12.5 Qty. Used 6 4 4 Orientation Floor Down sides/top/bottom Side In Special 6" for middle Flue Diameter 372.0 372.0

Length (enter) 792.0 Wi dth (deep) 170.0 Equiv. Diam. 279.9 372.0 372.0 Disturbance Dist A 60.0 720.0 2844.0

A Diameters 0.21 1.94 7.65 Dist B 508.8 84.0 4020.0 B Diameters 1.82 0.23 10.81 Points Qty. Used 30 24 12 Matrix Enter x Deep 6 x 5 6 x 4 4 x 3 Far Point Diatance 153.0 132.4 110.1

Reach 194.5 144.4 122.6 Probe (ft) 16.2 12.0 10.2 Time Run (min) 180
- 180

per Point 6 #VALUE! 15 Data minutes 3 5 Sample Volume dscf 137.7 137.7

acf 153.0 #VALUE! 153.0 Vlc 294.5 484.6 mg 15.1 #VALUE! 19.6 Rate, acfm 0.85 0.85 0.85 Increase Factor 2.6 #VALUE! 2.6 Grain Loading gr/dscf 0.0011 0.0070 .0009 - .0034 DP history 0.554 0.387 0.59 - 0.675 Ts history 288-325 137 132-135 Bws history 0.11 .186 (sat) 15.4-17.3 (sat) O2 history 6.2-6.8 6.3 6.5 - 6.9 SO2 history 312 1.51 1.1 Pst history 3.0-4.0 -1.3 - -1.65 -0.82 Notes CEMS Probe unheated unheated

Diluents CEMS
- bags (4) SO2 Strats Instrument CEMS CEMS

Time per point 5 6 Qty. Used 30 24 Total time 2.5 2.4 Statics Probes 1 4 (2 of Entec?)

Lines (1/4 poly) 1 @ 100' 200', 150', 2 @ 175' Runs 1 w/ outlet 1 w/ inlet Time, min. < 30 < 30 Personnel Sample Deck JC/KK DB/LK

Trailer GC/EG/BB/JF/SO GC/BB/JF/SO JF/BB/SO