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HomeMy WebLinkAboutNCD980557656_19990525_NC State University (Lot 86 Farm Unit 1)_FRCBERCLA LTRA_Air Dispersion Modeling March - May 1999-OCR, •. , . North Carolina State University .is •. grant university and a constituent institution . of The University of North Cmolina Office of Finance and Business Business Division An Equal Opportunity/Affirmative Action Employer Environmental Health & Safety Cen Campus Box 8007 Raleigh, North Carolina 27695-8007 March 25, 1999 Michael Townsend Superfund Branch, Waste Management Division US EPA Region IV Atlanta Federal Center I 00 Alabama Street, SW Atlanta, GA 30303-3104 http:/ /www2 ncsu. ed u/ncsu/eh s/ Director Environmental Affairs Industrial Hygiene Health and Safety Radiation Protection !Fax) Subject: NC State University Lot #86 Superfund Site -Air Dispersion Modeling Dear Mr. Townsend: This is to provide ten copies of the air dispersion modeling report, "Dispersion Modeling Analysis for N.C. State University, Lot 86 Site Raleigh, North Carolina." The copies of the report sent under cover of my March 18 letter to you lacked the model results tables and had other quality problems. Please accept my apologies for any inconvenience that this may have caused. Concerning model selection, I believe that SLAB is more applicable to the situation than either the ISC ST or SCREEN models. The principal parameters of this problem which define model selection are duration of release and spatial scale of the area of concern. The situation represented by the SLAB model is a short-term (accidental) release with receptors positioned very close to the source. With the puff releases at the Lot 86 site having a duration of about 15 seconds and the nearest fence! ine receptor being about 40 meters, it seems as though the SLAB model is the appropriate model for the situation. Both the !SC and SCREEN models are, at their core, Gaussian models. The Gaussian approach is based upon a continuous release. Gaussian-based dispersion models arc not designed to compute the dispersion and transport of a puff release. Similarly, because the SLAB model is intended for simulation of puff releases, it's spatial scale of "dependability" is measured in tens of meters. In contrast, the Gaussian models are best applied to receptors beyond the nearest receptor at Lot 86, of about 40 meters. Other specific issues that we discussed dealt with dense gas dispersion and designation of the release as a vertical jet. 919.515.423, 919.515.685, 919.515.686( 919.515.685, 919.515.289! 919.515.630: Michael Townsend March 25, 1999 Page 2 • • Dense gases. The SLAB model was originally designed to simulate the dispersion of dense gases. However, the model version used in this assessment contains a database of physical characteristics for a large number of gases, including density. For those chemicals which were not in the database, physical parameters required by the model were obtained from other sources. Therefore, the model uses actual contaminant density. Vertical jet. Simulating the release as a vertical jet was judged to be the most suitable release category. Observations of the puff releases shows that the release has enough buoyance ( exothermic reaction) to allow it to achieve a vertical profile of a few meters, before dispersing horizontally. However, the SLAB model simulated a surface release (release height~ 0 meters) to provide a conservative offsite concentration estimate. In conclusion, I believe that the SLAB model is appropriate for this application and that the model parameters provide a conservative estimate of off site contaminant concentration. I look forward to discussing this with you on March 30. S.irely, ~.___ Duane Knudson Enclosure • I-- ,_, --+-'fD_(jv~1_&__r ___ _ • ~~-~------f-~-_is __ C(_ __ ~fJ~rf--+t..-~-, -~ _ --+/....D.:t-_&'_6 __ [J_c5/.l!<t S~l-jpA._&Lo4J,1 _ ------+1~~)-~,-WJ_:_t:±-, __ -_J__-1./.l'JA.y-U..-< v'\-5-· --___ __,_,____\.'"':_,t)._l±,, _____ _ _________ ___,_..__ ___ --------------------• ____ _ +k--~-.R..~ 1"..>½.-\{-k"-~-• ~-S-~ !.j-/ J_, __ -~~-~-d,s c..<Md 42/, ________ _ -------!------------------ -----f--------------------- ----1-------±k-ci.......,(4 _____ _ -----------j .. ---·--------------------·----------- . 'ti;.!1 ·:. ~ .,/).'; ·:;;.-:}·;·,.- ·HuN/:'} R .~ :·, \: .;·. >··:·:.::_-,.· I, •, . . .. • . E·MCDEVI, \ RETARY • ..,oC} ' 'l) , 0 ,•., U ' 0 if' 0 • ' ·"J,Ji,'o LLIAM L. MEYB:R Cl ECT0~1 Jti' .si . ,. ' • • NORTH CAROLINA DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES DIVISION OF WASTE MANAGEMENT March 24, 1999 TO: David Mattison FROM: David Lilley '])-g L RE: Comments prepared on the Dispersion Modeling Analysis for NC State University, Lot 86 Site, Raleigh, NC March 17, 1999 After reviewing the above mentioned document, I offer the following comments: I. Page 8, last line: Change "Table 4-1" to "Table 3-1". 2. Page 13, first paragraph: Tables 4-1 through 4-3 have not been included in this report. Please submit them for review. DL/dl/word/ra 1/27 401 OBERLIN ROAD, SUITE 150, RALEIGH, NC 27605 PHONE 919-733-4996 FAX 919-715-3605 AN EQUAL OPPORTUNITY/ AFFIRMATIVE ACTION EMPLOYER -SO% RECYCLED/I 0% POST-CONSUMER PAPER • North Carolina State University.and· grant university and a constituent institution of The University of North Carolina Office of Finance and Business Business Division An Equal Opportunity/Affirmative Action Employer Environmental Health & Safety C· Campus Box 8007 Raleigh, Nonh Carolina 27695-8007 March 18, 1999 Michael Townsend Superfund Branch, Waste Management Division US EPA Region IV Atlanta Federal Center l 00 Alabama Street, SW Atlanta, GA 30303-3104 http: //www2. ncs u. ed u/ncsu/e hs/ Director Environmental Affairs Industrial Hygiene Health and Safety Radiation Protection {Fax) RECEIVED MAR 2 3 1999 SUPERFUND SECTION Subject: NC State University Lot #86 Superfund Site Dear Mr. Townsend: As promised in the March 8, 1999, letter from David Rainer, with this subject, enclosed are ten ( I 0) copies of the report, "Dispersion Modeling Analysis for N. C. State University, Lot 86 Site Raleigh, North Carolina." The modeling results support the University's contention that the "puff' releases of air borne contaminants from the site do not cause a risk to the public or the environment. Sincerely, Duane Knudson Enclosure ( l 0 copies) cc: David Mattison, NC DENR Grover Nicholson, NC DENR Mary Beth Kurz David Rainer 919.515.42 9t9.515.6f 919.515.6, 919.5156[ 919.515.2[ 919.515.6: ·• • • Dispersion Modeling Analysis for ' N.C. State University, Lot 86 Site Raleigh, North Carolina Prepared by: OMNI Professional Environmental Associates, P. A. P. 0. Box 13404 Research Triangle Park, North Carolina 27709 OMNI Project No. 99001 March 17, 1999 Section 1.0 Section 2.0 2.1 2.2 2.3 Section 3.0 3.1 3.2 ' ' J.J 3.4 Section 4.0 Table 2-1 Table 2-2 Table 3-1 Table 3-2 Table 4-1 Table 4-2 Table 4-3 Figure 2-1 Figure 2-2 Figure 3-1 Appendix A Appendix B Appendix C • • Table of Contents Introduction ............................................................................................................................... 1 Source and Site Description ............................................................................... ! ...................... 2 Site Description ......................................................................................................................... 2 Source Representation ............................................................................................................... 2 Chemical List ........................................................................................................................... .3 Modeling Methodology ............................................................................................................. 8 Model Selection Criteria ........................................................................................................... 8 Dispersion Model ...................................................................................................................... 8 Receptors ................................................................................................................................... 9 Meteorology .............................................................................................................................. 9 Air Dispersion Modeling Results ........................................................................................... 13 List of Tables Source Parameters ..................................................................................................................... 6 Hazardous Chemical List .......................................................................................................... 7 SLAB Model Options ............................................................................................................. 11 Fenceline Receptor Parameters .............................................................................................. 12 Comparison of Calculated Fenceline Concentrations with the NIOSH IDLH. ..................... 15 Comparison of Calculated Fenceline Concentrations with the OSHA PEL-Ceiling ............ 16 Comparison of Calculated Fenceline Concentrations with the OSHA PEL-TWA ............... 17 List of Figures Site Location ofN .C. State. Lot 86 NPL Site ........................................................................ .4 Potential Source Locations ....................................................................................................... 5 Raleigh. North Carolina Wind Rose ( 1987-1991) ................................................................ 10 Appendices Sample SLAB Model Input Files Sample SLAB Model Output ]:iles SLAB Model Output Figures • Section 1.0 Introduction • N.C. State University is performing a remediation of contaminated soil at its Lot 86 National Priorities List (NPL) Site using an in-situ mixing and encapsulation process. The Lot 86 NPL Site was formerly used as a disposal site for laboratory wastes, including hazardous wastes. As a result of technical impediments, the original mixing method, which included a shroud covering the mixing process, was replaced with open trench mixing and encapsulation. Although the open trench process is superior to the originally-selected method in terms of performance, it does allow for the airborne release of reaction products. During the course of the excavation and remediation activities, it became apparent that certain pollutants were being released to the atmosphere in "puffs" of short duration, typically no more than I 0-15 seconds. N.C. State has retained an environmental engineering consultant, OMNI Professional Environmental Associates, P.A. (OMNI Professional) to perform a dispersion modeling analysis of the puff releases. The purpose of this analysis is to determine, using the SLAB model, how the predicted fenceline concentrations of the monitored and detected airborne contaminants' compare with the applicable OSHA Permissible Exposure Limits (PEL) or other appropriate short-term exposure standards. The following sections present the sources and their surrounding area as they were represented in the dispersion modeling analysis, and the modeling methodology, and the modeling results. A few other chemicals, known to be present at the site but not detected in the air sampling, were included in the modeling analysis. Page I • • Section 2.0 Source and Site Description 2.1 Site Description The N.C. State University Lot 86 National Priorities List (NPL) Site 1s located in Raleigh, North Carolina. The site property is located between Wade Avenue and the State Fairgrounds, which are located to the north and south of the site, respectively. The closest off-site receptor consists of a 4 foot high construction fence, which is located along the northern boundary of the site, and is approximately 100 feet to the south of Wade Avenue. The northern boundary of the area to be excavated is approximately I 30 feet in lateral distance from the fenceline. The elevation of the northern ,:xcavation boundary is approximately I 0-15 feet higher than the elevation of the fenceline. Figure 2-1 shows the location of the facility and surrounding terrain. 2.2 Source Representation The portion of the site which remains to be excavated is a roughly rectangular piece of land, which rises approximately I 0-15 feet above the surrounding terrain. This area constitutes the area of occasional, potential puff releases of airborne contaminants. In order to deterrnine the worst-case fenceline concentrations of emitted contaminants, one potential source location was analyzed under worst-case meteorological conditions. The source has been placed on the northern boundary of the area to be excavated, at a point representing the shortest distance from a source to a potential off-site receptor. The source location is shown in Figure 2-2, and pertinent source parameters are listed in Table 2-1. An emission rate of I 00 g/s was used in the modeling analysis, as opposed to the I g/s rate proposed in the modeling protocol. The reason for this change is that the SLAB model was unable to provide quantifiable fenceline concentrations (i.e., concentrations were too small for the model to handle) when using an emission rate of I g/s. The concentrations obtained from modeling at an emission rate of 100 g/s were divided by a factor of JOO in order to obtain an effective fenceline concentration for an emission rate of I g/s. Page2 • • 2.3 Chemical List OMNI Professional used the results of the single reaction release sample provided in the Revised Monitoring Plan as the primary basis for determining the chemical parameters to be modeled. These contaminants are believed to be acceptable for environmental modeling because they are listed. Hazardous Air Pollutants (HAPs) under the Federal Clean Air Act. Four potentially hazardous chemicals which are believed to be present at the site, were added to the list. The list of chemicals to be modeled is shown in Table 2-2 Page 3 U.S.G.S. TCPCGR.APHIC WP RAJ...EICH 'NEST, N.C. QUAORANCLE DATED 1968. PHOTCRE'OS8 1987 OMNI PROFESSIONAL ENVIRONMENT AL ASSOCIATES, PA. N.C. State University Site 86 Location i.\'lap Raleigh, North Carolina Figure 2-1 P.O. Box 13-104 • Research Triangle Park. NC 27709 Scale: I" = 2,000' I OMNI PROFESSIONAL ENVIRONMENTAL Source and Receptor Locations NCSU Site86 ASSOCIATES, P.A. Raleigh, North Carolina P.O. Box 13-40..I • Research Triangle Park. NC 27709 Scale: I"= 100' • • • • Table 2-1 Source Parameters of the Emission Point N.C. State, Lot 86 NPL Site Source Parameters: Source A Discharge Height Above Ground Level (m) Discharge Type Source Area (m2): Exit Temperature (°K): Ambient Temperature (°K): Discharge Flow Rate (g/s): Discharge Duration (s): 0 Vertical Jet 1.0 298 298 100 15 Page 6 Detected Chemicals' Chloromethane Methylene Chloride Chloroform I, I, 1-Trichloroethane Benzene Carbon Tetrachloride Trichloroethene Toluene Tetrachloroethene Chlorobenzene Ethyl benzene Xylenes 1,3,5-Trimethylbenzene 1,2,4-Trimethylbenzene Freon-I 2 Chloroethane 1,2-Dichloropropane Styrene 1,2-Dichlorobenzene Added Chemicals Carbon Disulfide Methyl Ethyl Ketone Nitric Acid Ethylene Dibromide • Table 2-2 Hazardous Chemical List N.C. State, Lot 86 NPL Site • I. Chemicals detec1ed in the #2 Path and J-1 samples. listed in the Revised Final ,.-lir .\Joniroring Plan for the Xorth Carolina State University Lot 86 Site, dated 2/25/99. Page 7 • Section 3.0 Modeling Methodology 3.1 Model Selection Criteria • In order to ensure that the most accurate and reliable modeling data are obtained, OMNI Professional based its model selection on the following criteria: • The model must be capable of modeling short-duration or instantaneous releases of dense or neutrally-buoyant gases; • The model must have a low degree of error; • The model must produce consistent results; and • The model must allow the user to input meteorological conditions According to Uncertanties in Hazardous Gas Model Predictions, by Steven Hanna, when eleven air dispersion models (AFTOX, AIRTOX, B&M, CHARM, DEGADIS, GPM, HEGADAS, INPUFF, OB/DG, SLAB, and TRACE) were analyzed, the SLAB model demonstrated one of the smallest mean square errors, and produced the most consistent results of any of the eleven models for both instantaneous and continuous gas releases. The SLAB model also allows the user to input meteorological data. On the basis of these findings, OMNI Professional has decided to use Bee-Line Software's SLAB/or Windows 95. Version 5.00a for purposes of this dispersion modeling analysis. 3.2 Dispersion Model The SLAB model was run once for each of the specified chemicals using the distance between the potential source location and the fenceline receptor in order to determine the highest possible off-site concentrations. Worst-case meteorological conditions from the U.S. Environmental Protection Agency's (EPA) Offsite Consequence Analysis Guidance were assumed for modeling purposes (wind speed=l.5 mis: class F stability). ~ The SLAB modeling analysis was based on the specifications summarized in Table,4'.-1. Page 8 • • 3.3 Receptors The modeling analysis utilized a receptor, located on the northern fenceline. This receptor is located at a point representing the, shortest distance from a potential on-site source to an off-site receptor. The receptor parameters which were used in the analysis are listed in Table 3-2. 3.4 Meteorology The screening procedures for estimating impacts of the released chemicals on the receptor utilized the worst-case meteorological data for wind speed and stability from EPA's Ojfsite Consequence Analysis Guidance. The worst-case meteorological data corresponds to a wind speed of 1.5 mis, Class F atmospheric stability, and 50 percent relative humidity. A surface roughness height of 1.0 meters has been assumed (average surface roughness value for urban terrain, according to the SLAB On-Line Help Manual). An average wind measurement height of IO meters has been assumed. The wind was assumed to be blowing from the southwest (in a straight line between the source and the receptor) for each model run. A wind rose for Raleigh, North Carolina has been included in Figure 3-1. According to Figure 3-1, the wind in Raleigh. North Carolina blows from the southwest approximately 10 percent of the time. An ambient temperature of 298°K was used in the model runs. Page 9 WNW w \ \ WSW N NNW NNE 20% NW 15 I \ I \ 7.3% I \ j \ \ \ ·\ ,#~' I· I ' \ \~~ I ' I SW SSW SSE s . 3,.5 -5,5, ___ s.1115111·••1111.,0_1 -.:.o·..:o_-..:2:::,oc::==1•• ,-Fgl 2.0 -3,5 5.5 • 8.5 (M/Sec) NE ENE \ E I j I / ESE SE OMNI PROFESSIONAL ENVIRONMENT AL ASSOC!A TES, PA Raleigh, North Carolina Windrose (1987-1991) Figure 3-1 P.O. Box 13404 • Research Triangle Park, NC 27709 • • Table 3-1 SLAB Model Options -N.C. State Lot 86 NPL Site SLAB for Windows 95, Version 5.00a Option Surface Roughness Height Wind Speed Wind Measurement Height Atmospheric Stability Ambient Temperature Relative Humidity Selected Parameter I meter Worst-Case (1.5 mis)• 10 meters Worst-Case (Class F) • 298°K 50% * * Based on the U.S. EPA OCA Guidance Document (1996) for worst-case meteorological conditions. Page 11 • Receptor I: Fenceline Receptor • Table 3-2 Fenceline Receptor Parameters N.C. State, Lot 86 NPL Site Distance between Source A and Receptor I: 130 feet (39.6 m) Page 12 • • Section 4.0 Air Dispersion Modeling Results Fence line concentrations of the selected contaminants were evaluated using the source parameters given in Table 2-1, the modeling options given in Table 3-1, and the receptor parameters given in Table 3-2. The maximum predicted concentrations are listed and compared with the appropriate NIOSH IDLH, OSHA PEL-Ceiling, and OSHA PEL-TWA values in Tables 4-1, 4-2, and 4-3, respectively. The maximum predicted fenceline concentrations are well below the applicable IDLH values for all contaminants which have an assigned IDLH (see Table 4-1). The fenceline concentrations range from a minimum of 2x I 0·3 percent of the IDLH to a maximum of 8 percent of the IDLH, with a mean of 0.57 percent of the IDLH and a median of 0.12 percent of the !DUI. Based upon these results, it is unlikely that the fenceline concentrations of any of the contaminants modeled could exceed the IDLH values. The maximum predicted fenceline concentrations are also below the applicable OSHA PEL-Ceiling (PEL-C) limits for all contaminants which have an assigned PEL-C (see Table 4-2). The fenceline concentrations range from a minimum of 0.18 percent of the PEL-C to a maximum of 30 percent of the PEL-C, with a mean of 3 .62 percent of the PEL-C and a median of 0-45 percent of the PEL-C. Based upon these results, it appears unlikely that the fenceline concentrations of any of the contaminants modeled could exceed the PEL-C limits. The maximum predicted fenceline concentrations are below the OSHA PEL-TWA limits for all chemicals except for benzene and nitric acid. However, the PEL-TWA is an 8-hour average exposure, while the chemical "puffs" have a duration of 15 seconds or less. Thus, the fenceline concentrations of benzene and nitric acid, when averaged over a period of 8 hours, will be well below the applicable PEL- TWA. Three chemicals, chloromethane, Freon-12, and chloroethane, were not present in the SLAB chemical database. The fenceline concentrations of these chemicals were estimated by extrapolating from the Page 13 • fenceline concentrations of other chloromethanes (e.g., dichloromethane, trichloromethane (chloroform), and tetrachloromethane ( carbon tetrachloride)) and chloroethanes ( e.g., dichloroethane, trichloroethane). The results of the dispersion modeling analysis indicate that, at an emission rate of I g/s;·none of the chemicals detected in the air sampling at the Lot 86 NPL Site will exceed the applicable regulatory limits ( e.g., OSHA PEL-TWA, OSHA PEL-C, NIOSH IDLH) within the 15-second time frame of a release. Page 14 • • TABLE 4-1 Comparison of Calculated Fenceline Concentrations with the NIOSH IDLH Chemical Chloromethane (Methyl Chloride) Methylene Chloride (Dichloromethane) Chloroform 1, 1, 1-Trichloroethane• Benzene Carbon Tetrachloride Trichloroethene (Trichloroethylene) Toluene Tetrachloroethene (Perchloroethylene) Chlorobenzene Ethylbenzene Xylenes 1,2,4-Trimethylbenzene 1,3,5-Trimethylbenzene Freon-12 (Dichlorodifluoromethane) Chloroethane (Ethyl Chloride) 1,2-Dichloropropane Styrene 1,2-Dichlorobenzene Carbon Disulfide Methyl Ethyl Ketone Nitric Acid Ethylene Dibromide Mean': Median': Fenceline Cone. loom)' 1.82 3 1.00 0.55 0.50 1.50 0.30 0.50 1.00 0.35 0.80 0.70 0.80 0.70 0.70 0.30 3 0.98 3 0.70 0.90 0.15 1.40 1.80 2.00 0.12 0.84 0.80 IDLH' loom) 2,000 2,300 500 - 500 200 1,000 500 150 1,000 800 900 -- -- 15,000 3,800 -- 700 150 500 -- 25 100 1,674 600 Fenceline Cone. % of IDLH 0.09% 0.04%' 0.11% - 0.30% 0.15% 0.05% 0.20% 0.23% 0.08% 0.09% 0.09% ---- 2.00E-03% 0.03% -- 0.13% 0.10% 0.28% -- 8.00% 0.12% 0.57% 0.12% 1. Fenceline concentrations were obtained from the SLAB model, using an emission rate of 100 g/s. The concentrations were divided by 100 to estimate the fenceline concentrations for an emission rate of 1 g/s. 2. The IDLH (Immediately Dangerous to Life and Health) is an instantaneous exposure level which poses a hazard to human health. 3. Fenceline concentrations for these compounds was extrapolated from fenceline concentrations of other chloromethanes and chloroethanes. 4. Used 1, 1,2-Trichloroethane in the model, as data for 1, 1, 1-was not available. 5. Mean and median values were calculated using chemicals With IDLH values. "The lDLH concentrations were obtained from the NIOSH Chemical Listing and Documentation of Revised IDLH IDLH Values (As of 3/1195). These values were posted on the NIOSH Home Page (www.cdc.gov/niosh/idlh/intrid4.html). Page 15 • • TABLE 4-2 Comparison of Calculated Fenceline Concentrations with the OSHA PEL-Ceiling Chemical Chloromethane (Methyl Chloride) Methylene Chloride (Dichloromethane) Chloroform 1, 1, 1-Trichloroethane' Benzene Carbon Tetrachloride Trichloroethene (Trichloroethylene) Toluene Tetrachloroethene (Perchloroethylene) Chlorobenzene Ethyl benzene Xylenes 1,2,4-Trimethylbenzene 1,3,5-Trimethylbenzene Freon-12 (Dichlorodifluoromethane) Chloroethane (Ethyl Chloride) 1,2-Dichloropropane Styrene 1,2-Dichlorobenzene Carbon Disulfide Methyl Ethyl Ketone Nitric Acid Ethylene Dibromide Mean 7: Median': Fenceline Cone. lnnm)' 1.82 3 1.00 0.55 0.50 1.50 0.30 0.50 1.00 0.35 0.80 0.70 0.80 0.70 0.70 0.30 3 0.98 3 0.70 0.90 0.15 1.40 1.80 2.00 0.12 0.78 0.55 a PEL-Ceiling' loom) 200 ??? 50 - 5 (STEL)' 25 200 300 200 -· .. .. .. ·-.. .. .. 200 50' 30 .. .. 30 117 50 Fenceline Cone. % of PEL-C 0.91% .. 1.10% - 30.00% 1.20% 0.25% 0.33% 0.18% .. .. .. .. .. .. .. .. 0.45% 0.30% 4.67% .. .. 0.40% 3.62% 0.45% 1. Fenceline concentrations were obtained from the SLAB model. using an emission rate of 100 g/s. The concentrations were divided by 100 to estimate the fencefine concentrations for an emission rate of 1 g/s. 2. The PEL-C (Ceiling) is an exposure limit which is not to be exceeded at any time. 3. Fenceline concentrations for these compounds was extrapolated from fence!ine concentrations of other chloromethanes and chloroethanes. 4. Used 1. 1,2-Trichloroethane in the model. as data for 1, 1, 1-was not available. 5. The Short-Term Exposure Limit (STEL) is a 15•minute average exposure limit. 6. The 50 ppm Ceiling Limit is for the ortho (O·) isomer of DichloFObenzene 7. Mean and median values were calculated using chemicals with PEL·C (or PEL·STEL) values. • The OSHA PEL.Ceiling values were obtained from the 1998 edition of 29 CFR 1910.1000 (OSHA Standards for Air Contaminants), which was last revised 8/4/97. Page 16 • • TABLE 4-3 Comparison of Calculated Fenceline Concentrations with the OSHA PEL-TWA Chemical Chloromethane (Methyl Chloride) Methylene Chloride (Dichloromethane) Chloroform 1, 1, 1-Trichloroethane' Benzene Carbon Tetrachloride Trichloroethene (Trichloroethylene) Toluene Tetrachloroethene (Perchloroethylene) Chlorobenzene Ethylbenzene Xylenes 1,2,4-Trimethylbenzene 1,3,5-Trimethylbenzene Freon-12 (Dichlorodiftuoromethane) Chloroethane (Ethyl Chloride) 1,2-Dichloropropane Styrene 1,2-Dichlorobenzene Carbon Disulfide Methyl Ethyl Ketone Nitric Acid Ethylene Dibromide Mean': Median': Fenceline Cone. lnnm)' 1.82 3 1.00 0.55 0.50 1.50 0.30 0.50 1.00 0.35 0.80 0.70 0.80 0.70 0.70 0.30 3 0.98 3 0.70 0.90 0.15 1.40 1.80 2.00 0.12 0.87 0.80 PEL-TWA' loom) 100 ·- -- 350 1 10 100 200 100 75 100 100 -- -- 1,000 1,000 75 100 75 5 20 200 2 20 191 100 Fenceline Cone. % of PEL-TWA 1.82% - -- 0.14% 150.00% 3.00% 0.50% 0.50% 0.35% 1.07% 0.70% 0.80% -- -- 0.03% 0.10% 0.93% 0.90% 0.20% 7.00% 0.90% 100.00% 0.60% 14.19% 0.80% 1. Fenceline concentrations were obtained from the SLAB model, using an emission rate of 100 g/s. The concentrations were divided by 100 to estimate the fenceline concentrations for an emission rate of 1 g/s. 2. The PEL-TWA (Time-Weighted Average) is an eight-hour average exposure limit. 3. Fenceline concentrations for these compounds was extrapolated from fenceline concentrations of other chloromethanes and chloroethanes. 4. Used 1, 1,2-Trichloroethane in the model, as data for 1, 1, 1-was not available. 5. The 75 ppm TWA is for the para (p-) isomer of Oichlorobenzene 6. Mean and median values were calculated using chemicals with PEL-TWA values. * The OSHA PEL-TWA values were obtained from the 1998 edition of 29 CFR 1910.1000 (OSHA Standards for Air Contaminants), which was last revised 8/4/97. Page 17 S" f S'~ffifar t~ " .,_.,,L,,. , .. >i •J!,..,!,j,,c -~It,:,'-'· :.,.~(~fafX!!J!f;,1~~-·~~~f; ·:. • ,,,-"'.-_. __ ~ lC, , e. ~~f!~;{~ ~.\!\ . .Jlj\ 't"-1¥,,ru'".":r,f.: ;,;;I:"' :t!:J·,:1 ~~~ -,~~ • •';. ~:x ' ;,,l",,:::r~t'\;~ ,' ';', ; Ctib)( oionn -_-\",-'~ l" •• ,. __ ,__ -;: ..... , ... ~.4,,,/-t-~-fu~ . . · ,. 781":'lF""' .. ~-.i1~ •-· . ~--. -• J':i'<"--<::-,• ... ,, ·--~ "' ,, _<;.-.,'l;~~~;:-,r.n_-~~~~ .. ,,,;:, ~....,,,.,,,.,;:;::...JtJ.i;r~=~'!'~-s, __ .• -~~ __ ..=..;.. .... ;;.1~~c • ...._ • ~ _. ___ _, :f:'~,-,"l·:-t:,.·s,4'~,>",;:.~~i<::;"~ -e;'~~-:,a~~<l!~<'~'??,,::!· <-,'t,,:::,;: ~,~:";;':;,,;>• ''"'l4-'Z:> -I<--.,~ '7~ .. :,.,;;Jc>::,;~•,•;--t'-c>::'S"':""'- (I -~ ... i,~1Ytl!ic~'$iMitl;{f ·, ;,;.~ · .. :, :i:¼r!fu1"d~-~tt __ , • • Dichloromethane • Distance(m) Concentration(eemJ 1. 0000, 1000000.000 1. 0000, 1000000.000 1. 0124, 1728.112 1.0264, 1334. 724 1.0421, 1152.953 1.0597, 1037.302 1.0795, 953.057 1.1018, 886.845 1.1268, 832.229 1.1550, 785.642 1.1866, 744.909 1.2221, 708. 613 1.2621, 675.779 1.3070, 645.706 1.3575, 617.874 1.4143, 591.880 1.4781, 567.404 1.5498, 544.183 1. 6304, 521.992 1. 7209, 500.628 1.8228, 479.898 1.9372, 459.603 2.0659, 439.518 2.2105, 419.350 2.3730, 398.649 2.5557, 376.525 2.7610, 350.003 2.9919, 307. 626 3.2Sl3, 295.866 3.5429, 236.883 3.8707, 2,9.208 4.2391, 2/2,287 4.6532, .265.849 5.116i, 259. 738 5.6419, 253.850 6.2300, 2~8 .116 6.891!, 2"2.484 7. 6341, 236.915 8.4692, 231.375 9.4080, 225.841 10.4631, 220.290 11.6492, 214.706 12.9823, 208.405 1'1.4486, 193.767 16.0283, ~35.058 17.7306, l:"6.932 19.5661, :63.885 21.5470, 100.712 23. 6869, '52.293 26.0017, !..JJ.556 28.5097, 134.482 31.2318, i;•5. 122 34.1923, '15.587 37.4194, 106.023 40.9455, 96.586 44.8081, 57.421 49.0508, 78.646 53.7236, 70.348 58.8848, 62.584 64.6019, 55.387 70.9530, 48.768 Chloroform Distance(m) l. 0000, l. 0000, 1.0124, 1.0264, 1.0421, 1.0597, l. 0795, 1.1018, 1.1268, 1.1550, 1.1866, 1.2221, 1.2621, 1.3070, 1.3575, 1.4143, 1.4781, 1.5498, 1. 6303, 1.7209, 1.8228, 1.9372, 2. 0659, 2.2105, 2.3730, 2.5557, 2.7610, 2.9918, 3.25i3, 3. 5429, 3.8707, 4 .2391, 4. 6532, S.1187, 5.6419, 6.2300, 6.8911, 7.6341, 8.4692, 9.4080, 10.4631, 11.6492, 12.9823, 14.4807, 16.1293, 17.9057, 19.8193, 21.8808, 2-1.1023, 26.4972, 29.0811, 31.8716, 34.8891, 38.1570, 41.7024, 45.5564, 49. 7553, 54.3408, 59.3615, 64.8731, 70.9406, Concentration(ppm) 1000000.000 1000000.000 346.636 338.279 329.909 321.547 313.215 304.932 296.714 288.577 280.531 272. 588 264.755 257.039 249.440 241. 960 234.595 227.342 220.192 213.135 206 .156 199.236 192.348 185.455 178.504 171.413 164. 041 156.083 146.535 127.624 123.905 120.750 117.914 115.276 112. 767 110. 343 107.974 105.638 103.318 101.000 98. 673 96. 328 93.957 91.261 85.543 82.066 78.806 75.577 72. 308 68.958 65. 4 97 61.905 58. 1 77 54.331 50. 4 03 46.446 ,J 2. 520 38. 682 34.981 31.456 28.136 • ----~ 0... 0... .__., C 0 +:; ('O .... -C Q) u C 0 u SLAB Centerline Plot 100000 ..... 10000 1000 -.. · 100 10 ~-1··-·-··-·+ ·· •-··I··· · -·I· - 0 10 20 Fenceline I ! 30 40 Chemical Name: Dichloromethane Averaging Time: 15 s Fenceline Distance: 39.62 m ·I· -·-·--1· ~--· I· 50 60 70 Downwind Distance (m) • 80 • 1000000 ,-.. ~ 100000 (l_ (l_ § 10000 -ro .... -C Cl) u C 0 0 1000 101--~--------I· .... 0 10 SLAB Centerline Plot 20 Fenceline I 30 40 Chemical Name: Chloroform Averaging Time: 15 s Fenceline Distance: 39.62 m Toxic Endpoint: 100.42 PPM 50 60 Downwind Distance (m) • 70 80 • C 0 :.:, ro ,._ -C Q) u C 0 0 SLAB Centerline Plot 1000000 100000 · 10000 1000 • 100 10 ---~t--·~ . I -1 . ·-I - 0 10 20 Fenceline \ \ Chemical Name: 1, 1,2-Trichloroethane Averaging Time: 15 s Fenceline Distance: 39.62 m ------·---,--- :50 m 30 40 50 60 70 Downwind Distance (m) • 80 • ~ 0.... 0.... C 0 -rn L.. -C Q) (.) C 0 0 SLAB Centerline Plot 1000000 100000 10000 - 1000 -· 101--1-----1--1 -· ·-···1- 0 10 20 Fenceline I 30 -·,·----------------,-·----~ ' ' ' ' ' ' ' ' Chemical Name: Benzene Averaging Time: 15 s Fenceline Distance: 39_62 m ---·-· --------,------·-------- • 1.',() rr"' ' ' . --,--. -. - - - --- - ----,------- - - - ----- - I··· -----j---------1· ··---1----+----,----t----l 40 50 60 70 80 Downwind Distance (m) • • -----2 0.. 0.. ----C 0 :.:; ro '-+-' C Q) u C 0 u 1 000000 · · ----- 100000 · - 10000 1000 SLAB Centerline Plot i : I Fenceline l i i ' l I ; Chemical Name: Carbon Tetrachloride Averaging Time: 15 s Fenceline Distance: 39.62 m 1 :::_·-~t =.J. I-=--~I.~ .. ~.71~-=--~--~I -r-·:-11 ~10 ~ 11 :>m~I -:-1=--=··;:I. =··-=i-1 =-=··-·=-;:I=-·=-·+:~·-~· ~t~-=~-,. 0 10 20 30 40 50 60 70 80 90 Downwind Distance (m) • • ~ 0... 0... C 0 +-' C'll L.. +-' C Q) u C 0 0 SLAB Centerline Plot 1000000 100000 10000 1000 100 10 >--~f--·-· I -·--··I· -· ··-··I··-· 0 10 20 Fenceline I · : ,o ll 30 40 -·,-----~-~------,---------------. . . . . . . . Chemical Name: Trichloroethylene Averaging Time: 15 s Fenceline Distance: 39.62 m --------· ---,- -. . ' - -.,. --- - - --,-- : I ------1--·----1-.. --1 50 60 70 80 Downwind Distance (m) • • C 0 +-' co L.. +-' C Q) (.) C 0 0 SLAB Centerline Plot 1000000 100000 · 10000 1000 -· 100 10,-~,---·-·I ·-t-· · -1--··· t 0 10 20 Fenceli11e I 30 40 Chemical Name: Toluene Averaging Time: 15 s Fenceline Distance: 39.62 m . ;. ' ' I ·· ·-----1-----·-·t·· ·· · ---1----+----+>-----;•-----1 50 60 70 80 Dow11wind Distance (m) • • 1000000 · ----2 100000 0... 0.. -----C 0 ~ m L.. +-' C Q) (.) C 0 0 10000 1000 · .. 100 SLAB Centerline Plot Fenceli11e I -. ' ---------·--·-·,---------- ' ' ' ' Chemical Name: Tetrachloroethylene Averaging Time: 15 s Fenceline Distance: 39.62 m 10 >-~+-~1··----·--l----··--I·--· -•-I 0 10 20 30 40 50 60 70 Downwind Distance (m) • 80 • 1000000 ------'.:2: 100000 D... D... ---C 10000 0 :;:; ro I--1000 C (1) u C 0 100 0 10 SLAB Centerline Plot ... ---- 1------1·-----·--+· .... ·\··· .. · -1 --· 0 10 20 Fenceline) ) 30 40 Chemical Name: Chlorobenzene Averaging Time: 15 s Fenceline Distance: 39.62 m : 50 60 70 Downwind Distance (m) • 80 • C 0 :;::; Cl] L--C Q) u C 0 0 SLAB Centerline Plot 1000000 --- 100000 10000 1000 • Fenceline I Chemical Name: Ethylbenzene Averaging Time: 15 s Fenceline Distance: 39.62 m ,. "•- -' -- 100 ---~--~ ... :--. -::-~--~------r-70...:.:,ff_j;l~~~---..i··,-.:...· -~---~·-·:.:.:··-~---[,---~-- 10 ~--1------i --· i ---·t· -· ·I 0 10 20 30 40 50 60 70 Downwind Distance (m) • 80 • ~ 0.. 0.. C 0 -~ -C Q) (.) C 0 0 1000000 100000 10000 · 1000 · .... ,. 10·----1---1 0 10 SLAB Centerline Plot . . 1- 20 ' ' ' ' I Fenceline I : . I 30 40 Chemical Name: M-Xylene Averaging Time: 15 s Fenceline Distance: 39.62 m ···,·-· ------------, - - 1 - ---- - - -------"i - - - - - --- - - ·· + ·--·· I -------\1----i----+----t-- 50 60 70 80 Downwind Distance (m) • • ~ Q_ Q_ C 0 :;::; ro ._ +-' C Q) u C 0 0 SLAB Centerline Plot 1000000·-- 100000 10000 1000 _- 100 ;-------- 1 O>--~ ------·-! ------1-------1--------I 0 10 20 F~nceline I : Chemical Name: O-Xylene Averaging Time: 15 s Fenceline Distance: 39.62 m ; -. - - - --,--- - - - - - - - - - - - -,-- - - - - - - - - - - - -- - I· -1-------\------1-------f---f---+---t--~ 30 40 50 60 70 80 Downwind Distance (m) • • 1000000 ,......._ 100000 ~ 0.. 0.. ~ C 10000 0 --co L---1000 · C Q) u C 0 100 · u 10 0 10 SLAB Centerline Plot 20 I Fenceline I : Chemical Name: 1,2,4-Trimethylbenzene Averaging Time: 15 s Fenceline Distance: 39.62 m : 7lJ pffY1 ----~--L -I-------!----------t · ------!-·---f--,---+:-------1 30 40 50 60 70 80 Downwind Distance (m) • • C 0 -~ -C a.> (.) C 0 0 SLAB Centerline Plot 1000000 100000 10000 1000 100 ---- 1 0 l--+------1-------1-------1-----·-·· I · 0 10 20 Fenceli11e [ \ 30 40 Chemical Name: 1,3,5-Trimethylbenzene Averaging Time: 15 s Fenceline Distance: 39.62 m ., . ----,-------------,---------------- 1----l--·-··---1----+--' 0 ---+--+, -~---' 50 60 70 80 Downwind Distance (m) • • ~ 0.. 0.. C 0 ·..:; cu '--C (l) u C 0 0 SLAB Centerline Plot 1000000 100000. I Fenceline I : 10000 · .. 1000 C •••• ' ---··--·-----·,-·----. ' ' ' ' ' ' ' ' Chemical Name: 1,2-Dichloropropane Averaging Time: 15 s Fenceline Distance: 39.62 m ------,-- 100 .. ~--:-:---~---------f: "1i~v1irrf1!' ~··.:.i· -~··-~· ~----===l···--· ·---·--·--· 10 --1---·-----!--· --\--·--·1--·-· I .. 1------·-l------1 ------f----+--t---t---j 0 10 20 30 40 50 60 70 80 Downwind Distance (m) • • C 0 :;::. ro ,_ +J C Q) u C 0 0 1000000 --.... 100000 · 10000 1000 100 10 ---I ~ ··I 0 10 SLAB Centerline Plot j Fenceline I ; Chemical Name: Styrene Averaging Time: 15 s Fenceline Distance: 39.62 m ---·--,--------· ------ .' . . -. -. -. ' 20 30 40 50 60 70 80 Downwind Distance (m) • • ,-.. ~ (L (L C 0 :;:; ro '--C Q) u C 0 0 1000000 -·-· I 100000 10000 1000 .... 100 - 10 0 10 SLAB Centerline Plot --1-----1-----I· 20 30 :\ Fenceline \ : 15 ff'" Chemical Name: O-Dichlorobenzene Averaging Time: 15 s Fenceline Distance: 39.62 m - - . -·, - - - - -- - -. - - '. - - ' ' I -----l-----1-----+------1---i.---+---t----+-----l 40 50 60 70 80 90 100 Downwind Distance (m) • • ~ Cl. Cl. C 0 -cu '--C Q) (.) C 0 0 SLAB Centerline Plot 1000000 100000 10000 1000 , · 1 0 ---1----·I--· · --1------1--· · I 0 10 20 Fenceline I i 30 40 . ·----,---------------,·----------· ' ' ' ' ' ' ' ' Chemical Name: Carbon Disulfide Averaging Time: 15 s Fenceline Distance: 39.62 m 50 60 70 80 Downwind Distance (m) • • 1000000. C •••• - --~ 100000-.· 0... 0... C 0 -ro '-- 10000 · SLAB Centerline Plot [ Fenceline I [ Chemical Name: Methyl Ethyl Ketone Averaging Time: 15 s Fenceline Distance: 39.62 m C Q) (.) C 0 0 1000 - 100 .... -.. --.---------~•Jl®'Jf,'._ ___ ~··~···c;··c.···..:··c.···-··•..:· ·..:· --- 10 ···-· ·I 0 · I· ··I······· I 10 20 I· ... ·· I .. ·-I . ·----1~--1-----+----'-----l 30 40 50 60 70 80 Downwind Distance (m) • • SLAB Centerline Plot 1000000 ,-... ~ 100000 0.. 0.. § 10000 ....., Cll L- Fenceli11e I Chemical Name: Nitric Acid Averaging Time: 15 s Fenceline Distance: 39.62 m Toxic Endpoint: 10.1 PPM J 1 :::-. _-_-_ -r-----~---t: Jiv'!"l'E.__~--r=-:--:· ·c.;· ·;..· ---: ·::.· ·c.· --,,-·,;;· ·;.· ·;:· ---:•::. ·· ·::.· -------. -----. [I~~ic E~dpoint 10-----1-----1-----I----··· I -----I -I ------1---l-------1~L1-----+---l----+--l 0 10 20 30 40 50 60 70 80 90 Downwind Distance (m) • • 2 0... 0... ----C 0 -~ -C Q) u C 0 0 SLAB Centerline Plot 1000000 ,. -- - 100000 - 10000 • 1000 100 - 1 1~-1----·· I -•-·--1 -----! 0 10 20 Fenceline I : Chemical Name: Ethylene Dibromide Averaging Time: 15 s Fenceline Distance: 39.62 m '---------------- -- - ---: -- . . .. 1-------1-------1----.----~•--1 30 40 50 60 70 Downwind Distance (m) • • ~ 0.. 0.. C 0 :;::; co L.. +-' C Q) (.) C 0 0 SLAB Centerline Plot .v, ~-~,!/ 0,1/i, }o l(;/rqt,J~~ IMatNe Co,t, d-{,/1{1),'Je{(,m~ 1000000 -·- 100000 · 10000 1000. 100·· - - -. ---' - 10 J __ ~-<··----·--·1--··-···-1··---·· - I 0 10 20 [ Fenceline [ i 30 40 Chemical Name: 1, 1-Dichloroethane Averaging Time: 15 s Fenceline Distance: 39.62 m • 1 • - - • - ' ' . . -- --,-- ---- - - - -- - - - --,-. - - - - -- - --- ' ' ' ' · I -----1-----1----f---t----+---t---1 50 60 70 80 Downwind Distance (m) • •