EPA/600/A-95/141 Intrinsic Bioremediation of Fuel Contamination in Ground Water at a Field Site Don H. Kampbell', T.H. Wiedemeier51, and J.E. Hansenc °R.S. Kerr Environmental Research Laboratory, Ada, OK 74820, bParsotts Engineering Science, Inc., Denver, CO 80290 "U.S. Air Force Center for Environmental Excellence, Brooks Air Force Base, TX 78235 Abstract A spill of gasoline occurred at an automobile service station in 1986. Oily phase residue in the subsurface has continued for the past eight years to release water soluble fuel hydrocarbons into the aquifer. The site was characterized for implementation of intrinsic remediation. The subsurface was a beach sand with sea shell fragments. Hie water table was near 1.3 meters below ground surface. Surface dimensions over the plume were about 200 meters downgradient and 60 meters in width. Three points to coincide with direction of ground-water flow were selected in the plume for water quality assessments. Both methane and trimethylbenzene were used as surrogate tracers to normalize loss of contaminants. Aerobic respiration and methanogenesis.accounted for most biodegradation obtained. Assimilation capacities of dissolved oxygen, ferrous iron, and methane distributions when compared to BTEX concentrations showed that the ground water has sufficient capacity to degrade all dissolved BTEX before the plume moves beyond 250 meters downgradient. Evidence obtained from loss of contaminants, geochemistry, and microbial breakdown chemicals showed that intrinsic bioremediation technology would be a viable option to restore the site. Kev Words: intrinsic remediation. BTEX plume, aerobic respiration, methanogenesis. Introduction A detailed characterization study was conducted during March 1994 at a fuel spill location on Patrick Air Force Base in Cocoa Beach, Florida. Core material and ground- water samples were collected and analyzed to predict the influence of natural attenuation on dissolved contaminant migration and attenuation. Technical protocol followed was reported by Wiedemeier et al. (1994).The remediation of contaminants in ground water is called intrinsic remediation which incorporates mechanisms of biodegradation, sorption, dilution, volatilization, dispersion, and advection. All of these processes can operate concurrently during field scale implementation of bioremediation technology. The respiration processes microorganisms used to bring about a reduction in total contaminant mass in ground water are aerobic respiration, denitrification, iron or manganese ------- reduction, sulfate reduction, and methanogenesis. These processes called intrinsic bioremediation are important contributors to benzene, toluene, ethylbenzene, xylenes (BTEX) removal from ground water. If oily phase residue is present in the subsurface, it can act as a continuing source of contamination. To demonstrate intrinsic bioremediation at field spill sites, the quantification of biodegradation of BTEX which arc major fuel constituents is very important Patterns and rates can vary from site to site. The loss of contaminants downgradient to our site characterized was used as evidence for the occurrence of intrinsic bioremediation. Spill Site About 700 gallons of unleaded gasoline was released into the subsurface in 1986 at an on-base service station location. The subsurface matrix consisted of beach sand containing sea shell fragments to a depth of about 7.5 meters below ground surface (bgs) where a confining marl formation was located. The water table was near 1.3 meters bgs and the downward gradient measured in monitoring point wells was 0.002 m/m. Slug testing indicated that average hydraulic conductivity was near 0.026 cm/sec. The average advective ground-water velocity was about 48 m/year assuming a sand porosity of 0.35. Using TOC fneasurements, a retardation factor of 2.6 was calculated'for benzene. The effective solute transport velocity was 18.3 m/year. Results The extent of the plume was measured by the BTEX dissolved in the ground water as shown in Figure 1. Surface area over the plume was about 200 meter long and 60 meter wide. Free-floating gasoline was not detected in any well sampled. Loss of Contaminants Point A as shown in Figure 1 was selected for the highest dissolved BTEX with points B and C at 38 and 98 meters, respectively, downgradient in the plume. BTEX lost to biodegradation is listed in Table 2. Methane produced from BTEX and TMB = (measured BTEX + TMP) x (0.78). Ground water isopleth maps for BTEX, dissolved oxygen, ferrous iron, and methane are shown in Figures 1,2,3, and 4 respectively. Both methane and trimethylbenzene (TMB) were selected as surrogate tracers. It was assumed that all methane was both stable and produced from BTEX components (Table 3). Our usual approach has been to use trimethylbenzene (TMB) as a recalcitrant compound to correct BTEX concentrations for dispersion, dilution, sorption, and volatilization. For some reason benzene was higher at point B than at point A which indicated that TMB was under this site conditions not entirely recalcitrant However, the TMB corrected toluene, ethylbenzene, and xylenes decreased 30 to 60 percent between point A and B which confirmed that biodegradation occurred (Table 4). Even though some biodegradation of TMB may have occurred the corrected values would underestimate the ------- percent BTEX biodegraded. Between points B and C the relative decrease in TMB had a reduction rate similar to BTEX. Therefore, we choose not to use TMB as a surrogate tracer and concluded that BTEX/TMB radios did not substantiate that intrinsic bioremediation occurred. Ground Water Geochemistry «« The redox potential at the site ranged from 54 to -293 mV. Low redox potential coincided with sampling points of high BTEX contamination, low dissolved oxygen, some ferrous iron, and elevated methane concentrations. Water temperature was a warm 26°C which suggested that bacterial growth, rates could be high. Total alkalinity ranged from 148 to 520 mg/L which would suffice to buffer pH changes caused by BTEX biooxidation reactions. pH's near 7 were in the optimal range of BTEX-degrading microbes. Nitrate was very low so denitrifvcation for BTEX removal was not viable. Sulfate at levels up to 86 mg/L was fairly high, but a relationship between sulfate and BTEX changes was not apparent. Hie water chemistry suggested that dissolved BTEX would be subjected primarily to aerobic respiration, iron reduction and methanogenesis. The distribution of dissolved oxygen is shown in Figure 2. Site areas with depleted dissolved oxygen coincided with areas of elevated BTEX which indicated that aerobic biodegradation was occurring. Background dissolved oxygen was 3.7 mg/L so based on the Table 1 stoichiometry the shallow ground water had an assimilation capacity of 1200 ug/L total BTEX (Table 5).. Ferrous iron distribution (Figure 3) in the site ground water showed a direct relationship with elevated total BTEX. Background of ferrous iron was near 0.1 mg/L while levels up to 1.9 mg/L were present in the plume. Based on the Table 1 stoichiometry, the iron reduction would have the capacity to assimilate at least 90 ug/L of the total BTEX. Replenishment of the ferrous iron from soil iron oxides could occur to increase iron reduction capacity. Methane distribution is shown in Figure 4. A direct relationship occurred between elevated methane and total BTEX concentrations which indicated that methanogenesis was occurring. Background methane was near 1 mg/L while the highest plume methane concentration was 14.6 mg/L. Assimilation capacity during methanogenesis based on stoichiometry would be at least 17,400 ug/L of total BTEX (Table 5). Actual methanogenic assimilative capacity could be much higher because the amount of carbon dioxide available was not included. Methane corrected BTEX concentrations at points A,B, and C also provided evidence that intrinsic bioremediation was occurring (Table 3 ). Assimilative Capacity The expressed BTEX assimilative capacity of the site ground water was 18,690 (ig/L (Table 5) based on stoichiometry and site geochemical data. Since the highest ------- dissolved BTEX concentration at the site was 7300 ug/L the ground water has sufficient capacity to degrade dissolved BTEX that partitions from the soil oily residual into ground water before the plume moves beyond 250 meters downgradient from the source. The remainder assimilative capacity could be consumed by other gasoline components such as aliphatic hydrocarbons. Microbial Breakdown Components A ground-water sample was collected at Point A (Figure 1) for analysis of phenols and aliphatic/aromatic acids. The technique involved liquid-liquid extraction, derivatization, and gas chromatography/mass spectrometry analysis. Major components detected were branched heptanoic and octanoic acids, trimethylbenzonic acids, dimethylbenzonic acids, and some lower molecular weight acids such as propinoic and butyric. The presence of these fatty acid components in the BTEX plume is further evidence that viable microbial biodegradation processes are functional at the site. Rate Constant A first order biological decay rate was calculated using methane as a surrogate tracer. We assumed that once methane is produced from the fuel biodegradation was stable and therefore can be used as a tracer. Table 2 lists methane corrected BTEX and the amount lost between the A,B, and C. points. The biodegradation line slope between points A and C approximates a first order process. The average decay rate using retarded solute transport velocity for total BTEX was 0.014 week"1. This was within the range reported by Wilson et al. (1994). Conclusion Three lines of evidence to identify intrinsic bioremediation at the site were loss of contaminants at field scale, geochemical data, and the presence of intermediate microbial BTEX breakdown products. Contaminant loss showed that natural attenuation was occurring. Ground water chemistry determined the relative importance of each operating natural attenuation mechanism. The presence of volatile organic acids showed that microbial biodegradation processes were viable. Aerobic respiration and methanogenesis accounted for the greatest mass of BTEX mineralized. Disclaimer The research described has not been subjected to the U.S. Environmental.. Protection Agency's review process. Therefore, an official endorsement should not be inferred. ------- References 1. Wiedemeier, T.H., D.C. Downey, J.T. Wilson, D.H. Kampbell, R.N, Miller, and J.E, Hansen. 1994. Technical Protocol for Implementing Intrinsic Remediation with Long-Term Monitoring for Natural Attenuation of Fuel Contamination Dissolved in Groundwater (draft). Air Force Center for Environmental Excellence, Brooks Air Force Base, Texas. 2. Wilson, B.H., J.T. Wilson, D.H. Kampbell, and B.E. Bledsoe. 1994. "Traverse City: Geochemistry and Intrinsic Bioremediation of BTX Compounds." In Proceedings of the Symposium on Intrinsic Bioremediation of Ground Water, August 30 - September 1,1994. U.S. Environmental Protection Agency, pp 94-102. ------- Table 1. Benzene Biodeeradation Reactions Aerobic respiration 7.502 + QH* = 6C02 + 3H20 Denitrification 6NO"3 + 6H+ + C6H6 = 6C02 + 6H20 + 3N2 Iron reduction 60H+ + 30Fe(0H)3 + C6H< = 6C02 + 30Fe2+ + 78H20 Sulfate reduction 7.5H+ + 3.75SO,2- + QH* = 6C02 + 3.75H2S + 3HzO Methanogenesis 4.5H20 + CA = 2.25C02 + 3.75CH4 Table 2. BTEX Mass Lost to Biodeeradation, mg/L Compound Point A Point B Point C Benzene 724 960 1 Toluene 737 17 2 Ethylbenzene 823 12 1 Xylenes *5020 120 15 Trimethylbenzene 750 28 3 Total BTEX + TMB 8054 1137 23 Measured methane 14000 8800 2140 Methane produced from BTEX & TMB 6282 887 18 ------- Table 3. Percent Loss Using Methane-Corrected Levels Compound Point B Corrected mg/L Biodegradation A to B % Point C Corrected mg/L Biodegradation B to C % Benzene 2008 0 4 100 Toluene 35 95 9 46 Ethylbenzene 24 97; 9 22 Xylenes 251 95 67 43 Total BTEX &TMB 2400 70 103 91 Table 4. Percent Loss Using TMB - Corrected Concentrations Compound " "Point B Corrected mg/L Biodegradation A to B % Point C Corrected mg/L Biodegradation B to C % Benzene 25710 0 9 99 Toluene 455 38 ' 19 0 "Ethylbenzene 321 61 19 0 Xylenes 3214 36 139 0 Trimethylbenzene 750 0 28 0 Table 5. Assimilative Capacity of Site Ground Water Aerobic Respiration 1200 ug/1 Ferric Hydioxide Reduction 90 Methanogenesis 17400 Total 18690 Highest total BTEX 7300 ------- Figure 1: Total BTEX in Groundwater Patrick AFB, Florida Groundwater Flow Direction EXTENT Of SOU CONtAMNAllON SOURCE Of OONW4NAT1GN 111** K*ALKBCCONCSNTRAJ!ON&i0lJ -100— (DfcSHED VA4BŁ NFERRfDj CONIOUR MERVAi - VAftAfti 0 «0 is Figure 2: Dissolved Oxygen in Groundwater Patrick AFB, Florida Groundwater Flow Direction Q2 *0.1 02 •0.1 03 09, .03 •0 0J2 '0.3 35 04 OSKXVED OKYGtN CONCENTRATION fmtfl.) UNI OF E-QUAi OtSSOCVlD QXK3€N CONC&TTRAIION |rr*gfi,| PUSHED **<* NF©WŁ DJ CONKX* WlilWM. - VAJWBil d:^>jto&$h\fcarrpbe0V3onl doc ------- Figure 3: Ferrous Iron in Groundwater Patrick AFB, Florida 0.4 4jQ_ Groundwater Flow Direction FBSOUS RON CONCSMRABON UNg OF tow. fHWOUS RON CONCENIMDON mgdJfJASHED mat MBMEDI CONTOUR MBMU-(Mni0L •0 iet Figure 4: Methane in Groundwater Patrick AFB, Florida Groundwater Flow Direction \A9 2.14 14.95 J4 3.49 • 7M 416 [S3t 2J1 3.?7 4,41 1.74 METHANE CONCENTRATION fmtfl) UK OF KSUAl fcCTHftWI CONCENIRAION tOASHED WHERE HFf RREOJ CONTOUR NTEPVAL - VARIABLE •0 o 4D d:\pubish\karrpbeff\don2 cdr ------- TECHNICAL REPORT DATA (Please read Instructions on the reverse before compietinf 1. REPORT NO. 2. EP A/600/A-95/141 3. RE 4. title and subtitle INTRINSIC BIOREMEDIATION OF FUEL CONTAMINATION IN GROUND WATER AT A FIELD SITE 5. REPORT DATE 6. PERFORMING ORGANIZATION CODE 7. AUTHORISI 1DON H. KAMPBELL, "T.H. WIEDEMEIER, & 3J.E. HANSEN 8. PERFORMING ORGANIZATION REPORT NO. 9. PERFORMING ORGANIZATION NAME ANO ADDRESS 1U.S, EPA, RSKERL, P.O. Box 1198, Ada, OK 74820 2Parsons Engineering Science, Inc., Denver, CO 80290 3U.S.A.F. Center for Environ Excellence, Brooks AFB, TX 78235 10. PROGRAM ELEMENT NO. 11. CONTRACT/GRANT NO. In-House RPDK2 12. SPONSORING AGENCY NAME AND ADDRESS Robert S. Kerr Environmental Research Lab. - Ada, OK U.S. EPA P.O. Box 1198 r\v TAann 13. TYPE OF REPORT ANO PERIOD COVERED 14, SPONSORING AGENCY CODE EPA/600/15 is." ŁuPpleme'nta"ry notes Poster presentation at the symposium on Bioremediation of Hazardous Wastes: Research, Development, and Field Fvaluatinn?;* Annus! R-10 IQQ1! R\/a Prnn|< fslY Pfnroorjjpqc pi |f-i|ichorl A spill of gasoline occurred at an automobile service station in 1986. Oily phase residue in the subsurface has continued for the past eight years to release water soluble fuel hydrocarbons into the aquifer. The site was characterized for implementation of intrinsic remediation. The subsurface was a beach sand with sea shell fragments. The water table was near 1.3 meters below ground surface. Surface dimensions over the plume were about 200 meters downgradient and 60 meters in width. Three points to coincide with direction of ground-water flow were selected in the plume for water quality assessments. Both methane and trimetbylbenzene were used as surrogate tracers to normalize loss of .contaminants. Aerobic respiration and methanogenesis .accounted for most biodegradation obtained. Assimilation capacities of dissolved oxygen, ferrous iron, and methane distributions when compared to BTEX concentrations showed that the ground water has sufficient capacity to degrade all dissolved BTEX before the plume moves beyond 250 meters downgradient. Evidence obtained from loss of contaminants, geochemistry, and microbial breakdown chemicals showed that intrinsic bioremediation technology would be a viable option to restore the site. 17' key WORDS ANO DOCUMENT ANALYSIS 2' DESCRIPTORS b,IOŁNTif IERS/OPEN ENOED TEAMS COSATI field,Group 18. DISTRIBUTION STATEMENT RELEASE TO THE PUBLIC 19 stcuR,Tufe»r'; ?i NO Of "AGES 9 20 security CLASS (This pot-,-¦ UNCLASSIFIED 11 PRiCF ^ * Form 2220-1 (R*v. 4-77} p«Evious fdition is ossoietc ------- |