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EDGEWOOD CHEMICAL BIOLOGICAL CENTER U.S. ARMY RESEARCH. DEVELOPMENT AND ENGINEERING COMMAND ECBC-TR-777 EVAPORATION RATES OF CHEMICAL WARFARE AGENTS USING 5 CM WIND TUNNELS IV. VX FROM GLASS Carol A. S. Brevett Christopher V. Giannaras John J. Pence Joseph P. Myers Robert G. Nickol SCIENCE APPLICATIONS INTERNATIONAL CORPORATION Gunpowder, MD 21010-0068 Bruce E. King Kenneth B. Sumpter Seok H. Hong H. Dupont Durst RESEARCH AND TECHNOLOGY DIRECTORATE June 2010 Approved for public release; distribution is unlimited. 20100923366 ABERDEEN PROVING GROUND, MD 21010-5424

20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Page 1: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

EDGEWOOD CHEMICAL BIOLOGICAL CENTER

U.S. ARMY RESEARCH. DEVELOPMENT AND ENGINEERING COMMAND

ECBC-TR-777

EVAPORATION RATES OF CHEMICAL WARFARE AGENTS USING 5 CM WIND TUNNELS

IV. VX FROM GLASS

Carol A. S. Brevett Christopher V. Giannaras

John J. Pence Joseph P. Myers Robert G. Nickol

SCIENCE APPLICATIONS INTERNATIONAL CORPORATION

Gunpowder, MD 21010-0068

Bruce E. King Kenneth B. Sumpter

Seok H. Hong H. Dupont Durst

RESEARCH AND TECHNOLOGY DIRECTORATE

June 2010

Approved for public release; distribution is unlimited.

20100923366 ABERDEEN PROVING GROUND, MD 21010-5424

Page 2: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

Disclaimer

The findings in this report are not to be construed as an official Department of the Army position unless so designated by other authorizing documents.

Page 3: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

REPORT DOCUMENTATION PAGE Form Approved

OMB No. 0704-0188 Public reporting burden for this collection of information is estimated to average 1 hour per response, including the time for reviewing instructions, searching existing data sources, gathenng and maintaining the data needed, and completing and reviewing this collection of information Send comments regarding this burden estimate or any other aspect of this collection of information, including suggestions for reducing this burden to Department of Defense. Washington Headquarters Services. Directorate for Information Operations and Reports (0704-0188). 1215 Jefferson Davis Highway, Suite 1204. Arlington. VA 22202-4302 Respondents should be aware that notwithstanding any other provision of law. no person shall be subject to any penalty for failing to comply with a collection of information if it does not display a currently valid OMB control number PLEASE DO NOT RETURN YOUR FORM TO THE ABOVE ADDRESS

1. REPORT DATE (DD-MM-YYYY)

XX-06-2010 2. REPORT TYPE

Final 3. DATES COVERED (From - To)

Aug 2006 - Sep 2009

4. TITLE AND SUBTITLE

Evaporation Rates of Chemical Warfare Agents Using 5 cm Wind Tunnels IV. VX from Glass

5a. CONTRACT NUMBER

DAAD13-03-D-0017 5b. GRANT NUMBER

5c. PROGRAM ELEMENT NUMBER

6. AUTHOR(S)

Brcvctt, Carol A. S.; Giannaras, Christopher V.; Pence. John J.; Myers. Joseph P.; Nickol, Robert G. (SAIC); King, Bruce E.; Sumpter, Kenneth B.; Hong, Seok H.; and Durst. H. Dupont (ECBC)

5d. PROJECT NUMBER

BA07TAS041

5e TASK NUMBER

5f. WORK UNIT NUMBER

7. PERFORMING ORGANIZATION NAME(S) AND ADDRESS(ES)

SAIC. P.O. Box 68, Gunpowder, MD 21010-0068 D1R, ECBC, ATTN: RDCB-DRC-M, APG. MD 21010-5424

8. PERFORMING ORGANIZATION REPORT NUMBER

ECBC-TR-777

9. SPONSORING / MONITORING AGENCY NAME(S) AND ADDRESS(ES)

Defense Threat Reduction Agency, 8725 John J Kingman Road, Fort Belvoir, VA 22060-6201

10. SPONSOR/MONITORS ACRONYM(S)

DTRA

11. SPONSOR/MONITOR'S REPORT NUMBER(S)

12. DISTRIBUTION / AVAILABILITY STATEMENT

Approved for public release; distribution is unlimited.

13. SUPPLEMENTARY NOTES

14. ABSTRACT The evaporation of VX from glass was studied as a function of temperature, drop size, and air How rate, using the same instrumentation as prior studies of sulfur mustard evaporation from glass, concrete, and sand. The evaporation rate increased with higher temperature and drop size; wind speed was not a significant factor. An empirical equation was determined that would allow for the calculation of the evaporation rate given the atmospheric conditions. The data collected provide input for the validation of empirical and physics-based models on the evaporation of agent designed by other authors, and are input for the VLSTRACK model, which predicts agent vapor concentrations as a function of environmental conditions.

15. SUBJECT TERMS

VX Glass Evaporation rate Wind tunnc

16. SECURITY CLASSIFICATION OF:

a. REPORT

u b. ABSTRACT

U c. THIS PAGE

U

17. LIMITATION OF ABSTRACT

UL

18. NUMBER OF PAGES

68

19a. NAME OF RESPONSIBLE PERSON

Sandra J. Johnson 19b. TELEPHONE NUMBER (include area code)

(410)436-2914 Standard Form 298 (Rev. 8-98) Prescribed by ANSI Std. Z39.18

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PREFACE

The work described in this report was authorized under Contract No. DAAD13- 03-D-0017. The work began in August 2006 and was completed in September 2009.

The use of either trade or manufacturers' names in this report does not constitute an official endorsement of any commercial products. This report may not be cited for purposes of advertisement.

This report has been approved for public release. Registered users should request additional copies from the Defense Technical Information Center; unregistered users should direct such requests to the National Technical Information Service.

Acknowledgments

The authors thank Drs. James Savage and Terrence D'Onofrio (U.S. Army Edgewood Chemical Biological Center) for program guidance and Christine Franklin (Science Applications International Corporation) for administrative support. Funding from the Defense Threat Reduction Agency is gratefully acknowledged.

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CONTENTS

1. INTRODUCTION 9

2. EXPERIMENTAL PROCEDURES 9

2.1 Wind Tunnel 9 2.2 Detection ofVX in the Wind Tunnel Effluent 10 2.3 Analysis of Neat Ton Container VX 11 2.4 Experimental Design and Data Analysis 12

3. RESULTS 12

3.1 Time to Plateau 12 3.2 Percentage Recovery 12 3.3 Evaporation Rates 13 3.4 Combined Effects 13

4. DISCUSSION 24

5. CONCLUSIONS 25

LITERATURE CITED 27

APPENDIX: WIND TUNNEL DATA 29

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FIGURES

1. Retention Times of Ethyl Methylphosphonofluoridate, 1 min. Internal Standard Bromofiuorobenzene, 2.1 min, and Hydroxymandelic Acid, Ethyl Ether, 3.4 min 11

2. Mass Spectrum of the 1.1 min Ethyl Methylphosphonofluoridate Peak 11

3. Vapor Concentrations for 1 uL Droplets of VX Evaporating from Glass at 35 °C. 18 SLPM, and 50 °C, 405 SLPM 14

4. Average Time to Reach a Plateau in the Evaporation Rate of VX from Glass 14

5. Actual vs. Predicted Plots for the Time Taken to Reach a Plateau for the Evaporation of VX from Glass 15

6. Scatterplot of Temperature, Drop Mass, Air Flow, %Recovery, and Raw Evaporation Rate 18

7. Cube Plot of %VX Recovered for Evaporation from Glass 18

8. Least Squares Regression Analysis of %VX Recovered Data as a Function of Temperature, Air Flow, Drop Size, Tunnel Identity, and Time to Plateau 19

9. Calculation of the Evaporation Rate for a 6 uL Droplet of VX Evaporating from Glass at 35 °C and 181 SLPM 19

10. Cumulative VX Vapor Recovered for 1 uL Droplets of VX Evaporating from Glass at 35 °C, 18 SLPM, and 50 °C, 405 SLPM 20

11. Cube Plot of the Raw Evaporation Rates for VX Evaporating from Glass 20

12. Actual vs. Predicted Plots for the Raw Evaporation Rates for VX on Glass 21

13. Relative Contributions of Degradation and Evaporation for the Loss ofVX from Glass 22

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TABLES

Parameter Estimates for Major Effects for the Time to Plateau during the Evaporation of VX from Glass 15

Conditions and Experimental Evaporation Rates for the Evaporation of VX from Glass 16

Parameter Estimates for the Major Effects Contributing to the Raw Evaporation Rate for the Evaporation of VX from Glass 21

Comparison of Predicted and Measured Raw Evaporation Rates for the Evaporation of VX from Glass 23

SCHEMES

V-to-G Conversion on Silver Fluoride Pads 10

Degradation Pathways for VX 25

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EVAPORATION RATES OF CHEMICAL WARFARE AGENTS USING 5 CM WIND TUNNELS

IV. VX FROM GLASS

1. INTRODUCTION

The evaporation rates of the chemical warfare agent sulfur mustard from glass, concrete, and sand as a function of temperature, drop size, and air flow rate have been previously reported.1 "J Select evaporation and degradation rates of ton container VX on sand and glass have also been reported in the literature.4 In this work, additional evaporation data for VX on the same glass, as used previously, as a function of temperature, drop size, and air flow rate measured in 5 cm wind tunnels are presented. This report describes the data analysis and demonstrates the robustness of the set of data that will be passed to the modelers for eventual incorporation into field models such as VLSTRACK, which predicts vapor concentration as a function of environmental conditions.

2. EXPERIMENTAL PROCEDURES

2.1 Wind Tunnel

The 5 cm wind tunnels that were used in the present investigations have been previously described and were the same as those used for similar earlier studies on glass/ The design of the 5 cm laboratory-sized wind tunnels6 and the wind tunnel characteristics compared to other wind tunnels and outdoors measurements have been published. In order to expose the agent to the wind flow, the piston was removed and the test substrate (a 1.5 in. diameter circle) with the droplet of agent on it was placed onto the piston and inserted into the wind tunnel. The humidified, temperature-controlled air from a Miller-Nelson Environmental Control Unit (ECU) (tunnel a) or an Aalborg MFC (tunnels c, d, k, 1) was then passed over the sample and the vapors were collected on Markes TenaxR thermal desorption tubes (Agilent Technologies, Santa Clara. CA) at the vapor sampling inlet. The amount of agent on each tube was measured based upon a standard in the Gas chromatography/Mass Spectrometry (GC/MS). The sample volume and tunnel air flow rate were known; thus, the agent concentration (mg/nr) and evaporation rate (ug/min) could be calculated. The rates were not calculated for the initial 5 min of the experiment (before the instrumentation reached equilibrium) nor at the end of the experiment (when concentration of mustard was nearing a plateau due to sample exhaustion). Hence, the data in the middle of each experimental run were used to calculate the evaporation rates.

Air flows were 18, 181, and 405 standard liters per minute (SLPM), which corresponded to velocity values at a I cm height of 0.22, 1.7, and 3.6 m/s. The flow volume per thermal desorption tube was typically 2 to 10 L volume, and the tubes were automatically switched using a proprietary Versatile Tube Sampler. The rate at which the tubes were switched was adjusted based upon the evaporation rate of the agent. The air and substrate temperatures investigated in this work were 35, 42, and 50 °C, and the droplet sizes were 1, 6, and 9 uL, corresponding to droplet diameters of 1.24, 2.25, and 2.58 mm and contamination densities of

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approximately 1.3, 7, and 11 g/m". The droplets masses used in the calculations and tables were based upon the pipette setting; the samples were not weighed.

In general, the evaporation of the VX was measured until no further decrease in the concentration of vapor was detected at which time the experiment was terminated. Summation of the concentrations over time yielded the cumulative amount of VX that had evaporated. The data collected are shown in the Appendix.

2.2 Detection of VX in the Wind Tunnel Effluent

For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK) to convert any VX in the stream to its G-analog, ethyl methylphosphonofluoridate (EMPF, EA-1207) which is more volatile and therefore easier to analyze by thermal desorption GC. The chemical equation for the reaction is shown in Scheme 1.

O C3H7 O C3H7

H3C—P—S—CH2CH2N + AgF • H3C—P—F + AgSCH2CH2N

OC2H5 C3H7 OC2H5 C3H7

Scheme 1. V-to-G Conversion on Silver Fluoride Pads.

The ethyl methylphosphonofluoridate was desorbcd from the thermal desorption tubes using a Markes UNITY/ULTRA Desorption system (Markes International, Llantrisant, UK), and analyzed on an Agilent 6890/5973 Gas Chromatography/Mass Spectrometry Detector (GC/MSD [Agilent Technologies, Santa Clara, CA]) using a HP-5MS capillary column (30 m long, 0.25 mm id, 0.25 um film thickness, (5%-phenyl)-methylpolysiloxane stationary phase).4

Oven parameters were 60 (1.5 min) to 250 °C at 50 °C/min. Thermal desorber parameters were a tube desorption temperature of 250 °C for 2.5 min and a 10 mL/min split flow. The tube purge/sweep flow was 50 mL/min, the trap desorption temperature was 300 "C for 2.0 min. The sample was carried into a split/splitless injection port at 250 °C. The split vent was turned on at 0.5 min with a purge flow of 50 mL/min of helium. Retention times were I min for ethyl methylphosphonofluoridate, 2.1 min for the internal standard bromofluorobenzene, and 3.4 min for 3-hydroxymandelic acid, ethyl ether (impurity, not from VX) (Figure 1). The mass spectrometer was operated in Electron Ionization (El) mode and scanned from 35-300 amu in 2.78 s. The molecular ion for ethyl methylphosphonofluoridate (m/z = 126) was not typically observed, but the characteristic fragment ion at m/z = 99 was observed (Figure 2).

The ability of the Tenax TA tubes to collect the VX vapor was verified by injecting a known amount of VX vapor into a 20 ft copper tube that had flowing air and showed that the VX was quantitatively recovered.

10

Page 13: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

1.8E7

g 1 4E7 i S 1 0E7 i /

0.6E7 I |

1.00 2.00 3 00 4.00 5 00 3 00 4 00

Time An in

6 00

Figure I. Retention Times of Ethyl Methylphosphonofluoridate (MEPF), 1 min. Internal Standard Bromofluorobenzene (BFB), 2.1 min, and Hydroxymandelic Acid. Ethyl Ether. 3.4 min.

39

2E6

IE6

81

47 67 125 UL4-

Scan12(1 152 min) 10240001 D

111

r+- 10 160 180 266' 220' 240' 260' '280 300

Figure 2. Mass Spectrum of the 1.1 min Ethyl Methylphosphonofluoridate Peak.

2.3 Analysis of Neat Ton Container VX

Two samples were prepared for analyses by GC/MSD. The first sample was prepared by adding 2 uL VX to 200 uL of acetonitrile. From this dilute mixture, a 10 uL aliquot was further diluted into 0.6 mL of methylene chloride, which was analyzed by GC7MS, of which

1 pL was injected onto the GC/MS. The compounds of interest detected were 2- (diisopropylamino)ethanol, 12.1 min; diethyl dimethylpyrophosphonate, 16.2 min; VX. 20.0 min; and bis(diisopropylaminoethyl) disulfide, 23.5 min.

The second sample was prepared by adding 2 uL BSTFA and 2 uL VX to 200 uL acetonitrile. The mixture was then heated at 60 "C for 20 min. After the heating period. 10 pL of the derivatized mixture were added to 0.6 mL of methylene chloride and the resulting solution (1 pL) was analyzed by GC/MS. Compounds of interest detected were trimethylsilyl (TMS)- derivatized-ethyl methylphosphonic (EMPA)acid, 1 1.5 min; 2-(diisopropylamino)ethanol. 12.1 min; TMS-derivatized-ethyl mcthylphosphonothioic (EMPT) acid, 12.4 min;

I 1

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S-trimethylsilyl-2-(diisopropylamino)ethanol, 16.0 min; diethyl dimethylpyrophosphonate, 16.2 min; VX, 20.0 min and bis(diisopropylaminoethyl) disulfide 23.5 min.

2.4 Experimental Design and Data Analysis

The data were analyzed using JMP" Statistical Discovery Software. The three variables were temperature, drop size, and air flow rate at three levels each. Measuring all combinations of these levels would yield 27 conditions (3 x 3 x 3); the cubic composite design chosen required nine conditions, which can be described as the vertices of a cube and the cube's center. This collection of data allowed for the determination of the major contributing variables and interactions among variables, although in this particular study, not all of the data points in the experimental design were collected due to the length of time of each experiment. The substrate temperature (°C), droplet mass (mg), air flow (SLPM), total percent VX recovered, and tunnel identity (four similar 5 cm tunnels, named a, c, k and 1, were available) were treated as variables that may affect the raw evaporation rate. Effect interactions among droplet mass, air flow, and temperature were included in the numerical analysis.

3. RESULTS

3.1 Time to Plateau

The VX vapor was collected until the concentration of agent reached a plateau, often ~1 x 10" mg/m . The lowest detected vapor concentration was 2 x 10"1 mg/m (Figure 3). Only the 50 °C, 0.92 uL, 405 SLPM samples consistently gave vapor values of zero. The trend in the time taken to reach a plateau is shown in the cube plot in Figure 4. For many samples, the concentration at this time was near the short-term exposure limit (STEL required by the Occupational Safety and Health Administration [OSHA]) of 1 x 10 mg/m . A least squares regression (r = 0.94, radf = 0.91 )a showed that the significant factors were temperature, drop size (in mg), air flow, %VX recovered, tunnel 'a', and mass * air flow (Figure 5, Table 1). The equation generated was

Time to plateau = 6315 - 107*T + 145 * drop mass - 2.2 * air flow -7.2 * %VX recovered - 914 * tunnel[a] - 0.42 * {(drop mass - 4.3) * (air flow - 223)} (1)

3.2 Percentage Recovery

Scatterplots of the variables substrate temperature (°C), droplet mass (mg), and air flow (SLPM), and the results %VX recovered and raw evaporation rate showed that the %VX recovered and raw evaporation rate were loosely correlated with each other (r = 0.64,h Figure 6). None of the other parameters were correlated. In fact, the data showed that the %VX recovered and raw evaporation rate data were distributed throughout their respective ranges as a function of

a r estimates the proportion of the variation that can be attributed to the model rather than to random error: r,^ adjusts for models that have different numbers of parameters. A perfect fit is r = 1.0. JMP Statistics and Graphics Guide, Version 5, by SAS Institute, Cary, NC. 2002, pi86. r is the Pearson Product-Moment correlation; a perfect fit is r = 1.0. JMP Statistics and Graphics Guide, Version 5. by SAS Institute. Cary. NC, 2002, p376.

12

Page 15: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

temperature, drop mass, and air flow. A cube plot also shows the ranges in %recovery (Figure 7). The percentage of agent recovered was largely random; the least squares regression had a low correlation coefficient (r = 0.58, ra<if = 0.37, Figure 8).

3.3 Evaporation Rates

The evaporation rate was calculated by summing the %VX vapor recovered, plotting the cumulative %VX loss versus time, and taking the slope of the line, which was the evaporation rate (Figure 9). Examples of replicate collections of evaporation data at two different conditions demonstrate the degree of variability observed (Figure 10).

Given the large degree of variability in the raw evaporation rate (Table 2), the raw evaporation rates were divided by the %VX recovered to yield an adjusted evaporation rate. Organizing the data by condition and taking the averages showed that the adjusted evaporation rates covered a much smaller range than the raw evaporation rates, and major trends began to emerge, as shown in a cube plot (Figure 11, Table 2).

Numerical analysis of the data was performed - namely, using a least squares fit for the raw evaporation rates (mg/min) as a function of substrate temperature (°C), droplet mass (mg). air flow (SLPM), %VX recovered, tunnel identity and the interacting factors, temperature * mass, temperature * air flow and mass * air flow(Figure 12, Table 3). The r was 0.90; racy was 0.87, and the statistically significant factors were temperature, droplet mass (in mg), % agent recovered, temperature * air flow and drop mass * air flow; 40 datapoints were used. Tunnels 'a' and 'c' were significantly different from tunnels 'k' and T; and an equation was derived to represent the relationship (eq 2). A regression that included the %VX recovered yielded a lower r of 0.89. The least squares equation generated was then used to predict the evaporation rate for each sample (Table 4).

Raw evaporation rate = -8.08 x 10'*+ 1.41 x 10"4 * T + 4.05 x 10 4 * Drop mass +5.52 x 10" * %VX vapor recovered + 1.30 x 10"fl* (drop mass-4.4)* (air flow-207) +7.33 x 10"7* (T-42.6) * (air flow-207) +1.08 x 103 * tunnel[a] - 9.83 x 10"4 * tunnel[c] (2)

3.4 Combined Effects

The simultaneous effect of both degradation and evaporation was calculated. Degradation rates for VX on washed glass were calculated from the air-dried sand (ADS) values at 22. 30, 40, and 50 °C and the washed glass (WG) degradation rates at 22 °C for 97% or purer VX.4 At 22 °C, the ratio AWA'ADS = 0.0059/0.0181 = 0.325. The rate constants at 50 °C for ADS (0.0912 hr1) and the interpolated k at 35 °C (0.057 hr"1) were multiplied by 0.325 to give an estimate for the degradation rate on washed glass. Thus, the percentage of VX that had evaporated, degraded, and remained was plotted as a function of time for 35 and 50 °C (Fiyure 13).

13

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0.020

0.015 * x

CO 0.010 E ••D<>D ° *

0.000 %HWWi x

g 0.005

500 1000 1500 2000 2500

Time /mins

Figure 3. Vapor Concentrations for 1 uL Droplets of VX Evaporating from Glass at 35 °C, 18 SLPM (A,D,0,0), and 50 °C, 405 SLPM (x ,+,*,-)•

2800

3030

Drop size (1, 6, 9 uL)

2340

720

1850

2430

1380

344

900

Temperature 35,42, 50 °C

Wind speed 0.22,1.5 and 3.3 m/s

Figure 4. Average Time to Reach a Plateau in the Evaporation Rate of VX from Glass.

14

Page 17: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

3500-

3000-

§2500-

<2000-

£1500-

^1000-

500-

o-

800-

600-

.1

400-

o-

V 0 1000 2000 3000

Plateau Predicted P<0001 RSq=0.94 RMSE=312.35

(a)

4000

CO Z> •a CO I 200- 3 CO CD

5-200-

-400-

-600-

. 1

1000 2000 3000 4000

Plateau Predicted

(b)

Figure 5. Actual vs. Predicted Plots for the Time Taken to Reach a Plateau for the Evaporation of VX from Glass, (a) Least Squares Regression Fit (b) Residuals.

Table 1. Parameter Estimates for Major Effects for the Time to Plateau during the Evaporation of VX from Glass.c

Term Estimate Std Error Prob>jt| Intercept 6315 452 <0001 Temperature, T/°C -107 11 <0001 Drop mass /mg 145 31 0.0001 Air Flow rate/SLPM -2.2 0.7 0.0056 %VX recovered -7.2 2.9 0.0229 tunnel[a] -914 285 0.0044 tunnelfc] 324 198 0.118 tunnel[k] 215 141 0.144 (T-43.8)*(mg-4.3) -6.4 4.4 0.156

(T-43.X)*(SLPM-223) -0.02 0.10 0.833 (mg-4.3)*(SLPM-223) -0.42 0.12 0.0025

Values of Prob>|t| less than 0.05 are eonsidered significant.

15

Page 18: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Page 19: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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17

Page 20: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

50-

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43-75

13-50

Drop size (1, 6, 9 uL)

25-70

40-75

21-37

45-87

6-42

7-27

Temperature 33-114 35, 42, 50 X

Wind speed 0.22, 1.5 and 3.3 m/s

Figure 7. Cube Plot of %VX Recovered for Evaporation from Glass.

is

Page 21: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Figure 8. Least Squares Regression Analysis of %VX Recovered Data as a Function of Temperature, Air Flow, Drop Size, Tunnel Identity, and Time to Plateau.

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500 1000 1500 2000 2500 3000 3500 4000

Time (min.)

4500 5000 • Md-Time D Linear Linear (Linear)

Figure 9. Calculation of the Evaporation Rate for a 6 uL Droplet of VX Evaporating from Glass at 35 °C and 181 SLPM. The squares show the data that were used to generate the regression line of slope 0.0011 mg/min.

19

Page 22: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Figure 10. Cumulative VX Vapor Recovered for 1 uL Droplets of VX Evaporating from Glass at 35 °C, 18 SLPM (A,D,0,0), and 50 °C, 405 SLPM ( x,+,*,-). The solid line represents the degradation rate of VX at 50 °C and the dashed line represents the degradation rate of VX at 35 °C.

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3±1 35,42, 50 °C

Wind speed 0.22, 1.5 and 3.3 m/s

Figure 11. Cube Plot of the Raw Evaporation Rates (ug/min) for VX Evaporating from Glass.

20

Page 23: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Figure 12. Actual vs. Predicted Plots for the Raw Evaporation Rates for VX on Glass, (a) Least squares regression fit (b) residuals.

Table 3. Parameter Estimates for the Major Effects Contributing to the Raw Evaporation Rate for the Evaporation of VX from Glass.d

Term Estimate Std Error Prob>|t| Intercept -8.1 x 10"' 9.4 x 10"4 <0001 Temperature, T /°C 1.4x10"4 2.3 x 10s <.0001 Drop mass /mg 4.0 x 10"4 5.3 x 10*5 <.0001 Air flow /SLPM -1.0 x 10"(' 1.0x10"6 0.3004 %VX vapor recovered 5.5 x 10- 6.0 x lO" <.000l (T-42.6)*(drop mass-4.4) -8x 10"7 7.0 x 10"6 0.9106 (drop mass-4.4)*(air flow-207) 1.3 x 10"(1 2.6 x 10"7 <0001 (T-42.6)*(air flow-207) 7.3 x 10"7 1.5 x 10'' <.0001 tunnel[a] l.lxl 0-' 4.5 x 10"4 0.0219 tunnel[c] -9.8 x 10"4 4.3 x 10 4 0.0316 tunnehk 1.9 x 10 4 2.6 x 10"4 0.4716

' Values of Prot»|t| less than 0.05 are considered significant.

21

Page 24: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

100

80

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Time /mins Time /mins

• 50C degraded • 50C evaporated K 50C remaining D35C degraded • 35C evaporated B35C remaining

(a) (b) Figure 13. Relative Contributions of Degradation and Evaporation for the Loss of VX from Glass, (a) 50 °C (b) 35 °C.

22

Page 25: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

Table 4. Comparison of Predicted and Measured Raw Evaporation Rates for the Evaporation of VX from Glass.

Code Temperature/ °C

Drop mass/ mg

Air Flow/ SLPM

Raw Evaporation/ Rate

ug min '

Predicted Raw Evaporation Rate/

ug min ' 3k-016 34.5 0.92 181.7 0.33 0.23 3a-115 34.9 0.92 181.9 0.7| 0.76 3c-157 35.2 0.92 181.3 0.60 1.0 31-039 35.3 0.92 18.7 0.15 0.22 3k-037 35.3 0.92 18.7 0.11 0.57 3k-()29 35.5 0.92 18.8 0.12 0.45 31-030 35.5 0.92 18.8 0.01 -1.2 31-036 35.8 0.92 18.7 0.19 0.8 3k-023 49.6 0.92 405.6 4.3 5.3 3k-035 49.8 0.92 406.2 I.I 0.94 31-033 50.1 0.92 405.4 3.2 4.0 31-034 50.1 0.92 405.7 2.1 1.7 3k-025 50.2 0.92 405.6 2.1 1.9 3k-034 50.3 0.92 405.6 2.9 2.5 3k-027 50.5 0.92 405.6 3.1 2.7 3k-024 50.4 0.92 18.7 0.07 -0.29 3k-026 50.6 0.92 18.7 0.36 0.81 3k-022 34.5 5.51 181.7 1.03 1.5 3a-l16 34.6 5.51 181.9 0.75 0.70 31-020 34.8 5.51 181.6 0.58 0.0 3c-158 35.2 5.51 181.3 I.I 0.70 3k-028 41.4 5.51 181.7 7.2 6.2 3k-033 41.8 5.51 181.6 3.7 3.4 31-032 41.8 5.51 181.6 2.4 1.8 3k-038 42 5.51 181.6 2.6 3.2 31-037 42.2 5.51 181.5 3.2 3.7 3k-031 42.2 5.51 181.7 3.7 -i 2

31-027 34.7 8.27 405.4 3.9 3.3 31-031 34.7 8.27 405.4 1.4 2.1 31-038 34.9 8.27 405 2.5 2.2 3k-039 35.6 8.27 404.1 1.5 2.3 31-029 :o.5 8.27 18.7 0.39 1.0 31-035 50.7 8.27 18.7 2.0 2.3 3k-036 49.6 8.27 18.7 2.7 2.6 3k-032 50.1 8.27 18.8 1.7 2.1 31-022 50.5 8.27 18.7 0.26 0.37 31-026 50.6 8.27 18.7 4.7 4.4 31-021 50.1 8.27 405.4 5.0 5.4 31-023 50.7 8.27 405.4 4.0 5.1 31-025 50.6 8.27 405.5 8.9 7.5

23

Page 26: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

4. DISCUSSION

The precise reasons for the large, vexing variation in %VX recovered and raw evaporation rate remains unknown. The raw evaporation rate was derived from the cumulative %VX recovered. Thus, the loose correlation between %VX recovered and raw evaporation rate was not surprising. The least squares analysis used both %VX recovered and raw evaporation rate to generate the predictive empirical equation that had r = 0.90.

Since the drops were not individually weighed, the exact mass for each drop was not known, which would also add variability to the data. In addition, small changes in the amount of adventitious water present in the VX would affect the VX degradation rate, which would in turn affect the %VX recovered. Independent studies4 showed that the VX degraded with a half-life of 16 hr (960 min) at 30 °C, and 8 hr (480 min) at 40 and 50 °C. Thus, agent degradation was competing with agent evaporation in these experiments. Comparisons of the measured evaporation rates with the calculated degradation rates indicated that both processes occurred on a similar timescale. For the 50 °C samples, there was great variation in the cumulative %VX values (Figure 10), although evaporation for all samples had ceased at 400 min, indicating that all the VX had been exhausted. A mid-range sample was chosen for the comparison of the two processes. The calculated comparisons of evaporation and degradation at 50 °C in the bar graph indicated that VX would still be present at 600 min, but the vapor recovery in all cases indicated that the evaporation of the VX had ceased. This difference may indicate that the actual degradation rate was faster than the rate used in the calculations, possibly due to water in the air or EMPA in the VX. In addition, as the VX evaporated, the concentration of EMPA increased, thus increasing the degradation rate further in the autocatalytic cycle. As seen in Scheme 2, EMPA is both product and reactant for the degradation of VX. Thus, degradation rates in an open system may be faster than in a closed system at the same temperature. At 35 °C, the calculations indicated that VX would be present at 2400 min, as observed. The degradation rate was faster than the evaporation rate at 35 °C, whereas the evaporation rate was faster at 50 °C. The rate constants for degradation did not consider air flow or drop size effects, and thus only the temperature component is reflected in the bar graphs. In other words, with a different air flow or drop size, the evaporation/degradation balance will shift.

The EMPA formed is non-volatile; thus a mass-only method (such as balances or TGA) for following the evaporation of VX would be difficult, because the mass loss would be due to both VX and diisopropylaminoethyl thiol (DESH). As much as 3% EMPT product was detected in the NMR studies; the wind tunnel studies were not designed to detect the expected concomitant bis(2-diisopropylaminoethyl) sulfide product.

24

Page 27: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

o , II / o-p-s Me

n EM PA t-2

VX

66

O

Me-P=0

Me-P=0 i

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EMPT

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Me

EMPA

HS DESH

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.N.

S i

s.

H'

(DES)2

disulfide

sulfide

Scheme 2. Degradation Pathways for VX.4

5. CONCLUSIONS

During the first 1500 min, the VX vapors emanating from the glass substrate were above the Immediately Dangerous to Life and Health (IDLH) limit of 3 x 10" tng/m (IDLH is the Occupational Safety and Health Admininstration [OSHA] limit and the short-term exposure limit [STEL] of 1 x 10* mg/m ). Both degradation and evaporation were equally important contributors to the concentration decrease of VX vapors in these experiments. The exact point at which no further agent evaporated depended on the temperature, drop size, humidity of the air. and initial purity of the VX.

25

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Blank

26

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LITERATURE CITED

1. Brevett, C.A.S.; Giannaras, C.V.; Maloney, E.L.; Myers, J.P.; Nickol, R.G.; Pence, J.J.; King, B.E.; Sumpter, K.B.; Hong, S.H.; Durst, H.D. Evaporation Rates of Chemical Warfare Agents Using 5-cm Wind Tunnels. II. Munitions Grade Sulfur Mustard (H) from Sand: ECBC-TR-699; U.S. Army Edgewood Chemical Biological Center: Aberdeen Proving Ground, MD, 2009; UNCLASSIFIED Report (AD-A508 851).

2. Brevett, C.A.S.; Pence, J.; Nickol, R.G.; Myers, J.P.; Maloney, E.; Giannaras. C.V.; Flowers, A.; Sumpter, K.B.; Durst, H.D.; King, B.E. Evaporation Rates of Chemical Warfare Agents Using 5-cm Wind Tunnels. I. CASARM Sulfur Mustard (HD) from Glass; ECBC-TR-647; U.S. Army Chemical Biological Center: Aberdeen Proving Ground, MD. 2008: UNCLASSIFIED Report (AD-A493 238).

3. Brevett C.A.S.; Pence, J.J.; Nickol, R.G.; Myers, J.P.; Maloney, E.L.; Giannaras, C.V.; King, B.E.; Sumpter, K.B.; Hong, S.H.; Durst, H.D. Evaporation Rates of Chemical Warfare Agents Using 5-cm Wind Tunnels. III. CASARM Sulfur Mustard (H) from Concrete; ECBC-TR-745; U.S. Army Edgewood Chemical Biological Center: Aberdeen Proving Ground, MD. 2009; UNCLASSIFIED Report (AD-A516 459).

4. Brevett, C.A.S.; Sumpter. K.B.; Pence. J.; Nickol. R.G.; King. B.E.; Giannaras, C.V.; Durst, H.D. Evaporation and Degradation of VX on Silica Sand. ./. Phys. Chem. C. 2009, 113 (16), pp 6622-6663.

5. Weber. D.J.; Scudder. M.K.; Moury, C.S.; Donnelly, T.; Park, K.; D'Onofrio, T.G.; Molnar, J.W.; Shuely, W.J.; Nickol, R.G.; King, B.: Danberg. J.; Miller. M.C. Micro Wind Tunnel for Hazardous Chemical Fate Studies. In Proceedings of the 45th A/AA Conference. January. 2007; AIAA-2007-0960.

6. Weber. D.J.; Scudder, M.K.; Moury. C.S.; Shuely, W.J.; Molnar, J.W.; Miller, M.C. Development of the 5-cm Agent Fate Wind Tunnel; ECBC-TR-327, U.S. Army Edgewood Chemical Biological Center: Aberdeen Proving Ground, MD, 2006; UNCLASSIFIED Report (AD-A462 884).

7. Danberg, J. Evaluation of 5-cm Agent Fate Wind Tunnel Velocity Profiles; ECBC-CR-091; U.S. Army Edgewood Chemical Biological Center: Aberdeen Proving Ground. MD. 2007; UNCLASSIFIED Report (AD-A472 909).

8. Weber. D.; Scudder, M.K.; Moury, C; Shuely, W.; Molnar, J.; Danberg, J.F.; Miller, M. Velocity Profile Characterization for 5-cm Agent Fate Wind Tunnel; ECBC- TR-567; U.S. Army Edgewood Chemical Biological Center: Aberdeen Proving Ground, MD, 2007: UNCLASSIFIED Report (AD-A476 518).

9. Smith. J.E. Jr.; Boyd. W.D.; Mason, D.W. Depot Area Air Monitoring System and VX Study', Contract DAAK11-77-C-0087; Southern Research Institute: Birmingham, AL, 1982.

27

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10. Committee on Review and Assessment of the Army Non-Stockpile Chemical Materiel Demilitarization Program: Workplace Monitoring, National Research Council, Impact of Revised Airborne Exposure Limits on Non-Stockpile Chemical Materiel Program Activities; National Academy of Science: Washington, DC, 2005, p 37.

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Page 31: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Page 32: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Page 33: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Page 47: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Page 48: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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Page 49: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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APPENDIX 51

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APPENDIX 53

Page 56: 20100923366For the analysis of VX, a silver fluoride pad (CAMSCO, Houston, TX) was inserted onto the end of Tenax TA thermal desorption tubes (Markes International, Llantrisant, UK)

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APPENDIX 56

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APPENDIX 57

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