Accelerated Site Cleanup Using a Sulfate-Enhanced In Situ Remediation Strategy



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Accelerated Site Cleanup Using a Sulfate-Enhanced In Situ Remediation Strategy By: Sheri Knox, Tim Parker, & Mei Yeh YOUR NATURAL SOLUTIONS Patented Methods for In Situ Bioremediation

Slide 2 About EOS Remediation U.S.-based bioremediation company Proven products used worldwide Every continent except Antarctica Green states & provinces - EOS implemented

Slide 3 Our Family of Products Soil & Groundwater Bioremediation Products Category Product Name Target Contaminants Biostimulation (Anaerobic) EOS EVO AquaBupH VOS (under development) Chlorinated Solvents Perchlorate Chromate Explosives Radionuclides Acid Mine Drainage Biostimulation (Aerobic) Bioaugmentation EAS EOx BAC-9 ENV-TCA20 PJKS-1 Petroleum Hydrocarbons Petroleum Hydrocarbons Chlorinated Solvents Chlorinated Alkanes Chlorinated Solvents

Slide 4 Presentation Overview Introduction to Bioremediation What is EAS? Why add sulfate? What contaminates can be addressed? Case Study Conclusion

Slide 5 In Situ Bioremediation In Situ Bio Remediation In Place Microbial Method to Fix Microorganisms are used to Clean up Pollution in the Environment Reference: Lisa Alvarez-Cohen, Civil and Environmental Engineering University of California, Berkeley, Earth Science Division, LBNL

Slide 6 Microbial World: The Unseen Majority ~20,000 strains/species of bacteria in 1g topsoil Bacteria in 5g topsoil = ~total human population of Earth Total bacterial population of Earth = ~5 x 10 30 cells >90% of bacteria are in the subsurface below 30 feet Ref : Whitman et al. (1998) Proc. Nat Acad. Sci. USA 95: 6578-6583 Slide Courtesy of Greg Davis, Microbial Insights

Slide 7 How Does It Work? How does in situ bioremediation clean up pollution? Soil microbes are remarkably versatile! They eat (electron donor) and breathe (electron acceptor) many types of organic and inorganic chemicals to generate energy to live. (Gasoline, oil, chromium, iron, solvents, perchlorate, nitrate, ammonia, MTBE, etc) They live in complex communities capable of degrading many contaminants. Reference: Lisa Alvarez-Cohen, Civil and Environmental Engineering University of California, Berkeley, Earth Science Division, LBNL

Slide 8 How Does It Work? Growth-Promoting Biological Reduction + + Electron Donor (Food) Electron Acceptor (something to breathe) [O 2, NO 3, SO 4, TCE, etc.] EOx Waste Products [CO 2, N 2, FeS 2, Cl - ] Energy (Drawing Modified from AFCEE and Wiedemeier)

Slide 9 Applying In Situ Bioremediation Natural Attenuation biotransformation occurs naturally: indigenous microbes present, substrates & nutrients present (can be MNA) Biostimulation - indigenous microbes present, substrates &/or nutrients must be added Bioaugmentation indigenous microbes not present, organisms are added

Slide 10 Why Bioremediation? Remediation Costs: Enhanced Bioremediation $29/yd 3 Thermal Treatment $88/yd 3 Chemical Oxidation $125/yd 3 Surfactant Co-solvent Flushing $385/yd 3 From: McDade, Travis, and Newell, 2005. Analysis of DNAPL source-depletion costs at 36 field sites. Remediation Journal 15, 9-18.

Slide 11 What is EAS? Electron Acceptor Solution A soluble product for anaerobic biodegradation of petroleum hydrocarbon Stimulates microbial growth Patented Process (US Patent No. 7,138,060)

Slide 12 Typical Petroleum Release Reference; Kolhatkar, R and Taggart, D, 2004

Slide 13 Hydrocarbon Impacted Aquifers After Chapelle (2001)

Slide 14 Conventional Wisdom Add Oxygen High Energy Yield Fast Kinetics (Lab Experiments) Electron Acceptors Products 1. Oxygen >>> Water, CO 2 2. Nitrate >>> Nitrogen, CO 2 3. Fe(III) >>> Fe(II), CO 2 4. Mn(IV) >>> Mn(II), CO 2 5. Sulfate >>> Sulfide, CO 2 6. CO 2 or fermentation >>> Methane Aerobic Anaerobic Low Slow

Slide 15 Sulfate-Utilizing Microbes Dominate Process EPA-BP Study at 74 Sites sulfate reduction methanogenesis nitrate reduction aerobic oxidation iron reduction Ref: Wiedemeier, T.H et al. at 38 Sites AFCEE Study at 42 Sites

Slide 16 Why EAS? Electron Acceptor (EA) Maximum Concentration (mg/l) Mass of Benzene Degraded per Unit Mass of EA Potential Benzene Degraded (mg/l) Issues Oxygen (in air) 9 10 0.33 3.0 3.3 Limited solubility Pure Oxygen 60 70 0.33 19.8 23.1 Numerous oxygen sinks Potential aquifer clogging Biofouling near injection point EAS (A sulfate based soluble electron acceptor solution ) >1,000 0.22 >220 Hydrogen sulfide; never documented as an issue in the field

Slide 17 How Does EAS Work? Growth-Promoting Biological Reduction + + Electron Donor (Food) Electron Acceptor (something to breathe) [O 2, NO 3, SO 4, TCE, etc.] Waste Products [CO 2, N 2, FeS 2, Cl - ] Energy (Drawing Modified from AFCEE and Wiedemeier)

Slide 18 Sulfate-Reducing Bacteria (SRB) Reaction Petroleum Hydrocarbon + EAS + Dissolved Iron Iron Sulfide + H 2 O + MgCO 3 + CO 2 Iron Sulfide and Magnesium Carbonate are insoluble and immobile.

Slide 19 Why EAS Enhancement? Accelerates site cleanup In Situ Minimal Disruption & O&M Cost effective Green Technology Proven

Slide 20 Typical EAS Project Removed leaking tank Injection Point Inject EAS into contaminant plume Unsaturated zone Monitoring Wells Groundwater flow Saturated zone (Drawing Modified from ITRC and Koenigsberg 2007) Plume of dissolved contaminants

Slide 21 Contaminants that can be Treated with EAS Petroleum Hydrocarbons Aromatic Hydrocarbons Total Petroleum Hydrocarbons (TPH) Benzene, Toluene, Ethylbenzene, and Xylenes (BTEX) Methyl tert-butyl ether (MTBE) tert-butyl Alcohol (TBA)

Slide 22 How Much EAS is Required? Generally 3-4 EAS applications Utilization factor 4.7 grams of sulfate consumed per gram of BTEX degraded (Reference: Wiedemeier et al.)

Case Studies Courtesy of James F. Cuthbertson, Senior Consultant Delta Consultants, an Oranjewoud N.V. Company YOUR NATURAL SOLUTIONS Patented Methods for In Situ Bioremediation

Slide 24 Former Gasoline Service Station Potterville, MI Confirmed releases in 1992 and 2001 Prior remedies: High vacuum total fluids extraction, oxygen bio-sparging, bioaugmentaton & MNA Geology: Silty clay with granular fill material Perched groundwater 1 to 2 feet bgs Liquid phase hydrocarbon (LPH) was last encountered in March 2003 Sulfate enhancement was pursued as the lowest cost alternative to accelerate remediation and respond to a potential sensitive receptor (wetland area)

Slide 25 Potterville, MI Site Map OW-18 (Source Area / Tank Cavity)

Slide 26 Results Potterville, MI Source Area/Tank Cavity B,T,E,X vs. Sulfate 20,000 2,000 Benzene, Toluene, Xylene Concentration (ug/l) 18,000 16,000 14,000 12,000 10,000 8,000 6,000 4,000 2,000 1,800 1,600 1,400 1,200 1,000 800 600 0 4/6/2001 7/6/2001 10/6/2001 1/6/2002 4/6/2002 7/6/2002 10/6/2002 1/6/2003 4/6/2003 7/6/2003 10/6/2003 1/6/2004 4/6/2004 7/6/2004 10/6/2004 1/6/2005 4/6/2005 7/6/2005 10/6/2005 1/6/2006 4/6/2006 400 200 Sulfate Conc. (mg/l) Ethylbenzene Conc. (ug/l) Benzene Toluene Xylene Application Cleanup Target Ethylbenzene Sulfate 0 Date

Slide 27 Midland, MI Case Study Confirmed releases in 1988 and 2000 Primarily Sands with granular fill material to 8 feet bgs with clay to maximum explored depth Groundwater approximately 6 to 8 feet bgs

Slide 28 Midland, MI Site Map OW-19 (Compliance Well) OW-3AR (Within Treatment Zone)

Slide 29 Monitoring Well Within Treatment Zone Midland, MI Observation Well OW-3AR Sulfate vs. Total BTEX Concentrations Total BTEX Sulfate Applications Sulfate Concentrations 5,000 4,500 250 Total BTEX (ug/l) 4,000 3,500 3,000 2,500 2,000 1,500 1,000 200 150 100 50 Sulfate Concentration (mg/l) 500 0 0 02/06/03 05/16/03 07/30/03 11/14/03 02/24/04 05/03/04 08/17/04 11/10/04 01/11/05 06/28/05 08/02/05 11/01/05

Slide 30 Compliance Well 3,000.0 Midland, MI Observation Well OW-19 Sulfate vs. Total BTEX Concentrations Total BTEX Sulfate Application Sulfate Concentrations 160 2,500.0 140 Total BTEX (ug/l) 2,000.0 1,500.0 1,000.0 500.0 120 100 80 60 40 20 Sulfate Concentration (mg/l) 0.0 0 05/16/03 07/30/03 11/14/03 02/24/04 05/03/04 08/17/04 11/10/04 01/10/05 06/28/05 08/02/05 10/31/05

Slide 31 Example Closure / NFA Projects Gas Station, GA 1995 Release, Dissolved BTEX, EAS Application May 2008, NFA Granted October 2008 Bulk Terminal, VA 1993 Release, LPH Sheen, EAS Applications 2006 and 2007, Closure Granted October 2008 Gas Station, Washington, D.C. Dissolved BTEX and MTBE, EAS Application June 2008, NFA Granted July 2009 cost savings of > 55% Gas Station, Washington, D.C. Dissolved BTEX and MTBE, EAS Application June 2008, NFA Granted September 2009 cost savings of > 50%

Slide 32 Application Overview After an EAS TM application, sulfate levels initially rise and then decrease in conjunction with the reduction of contamination levels If the contaminant is still present and sulfate is at background levels, another application may be needed

Slide 33

Slide 34 Application Experience Applied at over 200 sites FL, CA, MI, IN, IL, WV, VA, IA, GA & NY Method of Injection & application Infiltration trenches Vertical wells Surficial spreading Former recovery wells Former SVE wells Temporary Geoprobe points Variety of geological and hydrogeological settings

Slide 35 Benefits of EAS Minimal site disruption In situ approach with no ongoing O&M activities Cost effective

Slide 36 Benefits of EAS Safe Green Natural Process

Slide 37 Benefits of EAS Accelerated cleanup Information gained significantly strengthens advocacy position with regulatory agencies Monitoring frequency showed no lag time for acclimation of native sulfate reducing bacteria

Slide 38 Overview of Patented Process US Patent No. 7,138,060 Issued November 21, 2006 Patent issued for: A process that enhances the environmental conditions existing within a contaminant plume by replenishing a natural groundwater compound required by bacteria to degrade the contaminants. Sulfate solution in excess of 1,000 ppm Covers all pollutants that can be degraded by sulfatereducing microorganisms

Slide 39 Conclusion Enhancement of biodegradation with the addition of EAS TM is a viable technique to safely and aggressively remediate BTEX, MTBE and petroleum impacted groundwater Design, implement and monitoring is a relative easy process

For more information, please visit: Thank you for attending Questions? J&L Environmental Technology CO., LTD 森 品 環 境 科 技 股 份 有 限 公 司 Contact: Kevin Liu ( 劉 瑞 文 ) Phone: (07) 6162. 000 kevin@jletco.com.tw www.jletco.com.tw YOUR NATURAL SOLUTIONS Patented Methods for In Situ Bioremediation Contact: Sheri Knox or Tim Parker Phone: 919.873.2204 sknox@eosremediation.com Skype: sheri.knox