EAS Presentation

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    EAS Presentation - Presentation Transcript

    1. Electron Acceptor Solution (EAS™) Sulfate Enhanced Anaerobic Bioremediation Contact: Craig Marlow 8248 Hidden Forest Drive Holland, Ohio 43528 Phone 419.867.8966 Fax 419.867.8976 Cell 419.349.7970 Email [email_address]
    2. About EOS Remediation
      • A leading, U.S.-based bioremediation company, with growing international scope
      • Our family of proven remediation products are available worldwide
        • U.S., Canada, South Africa, Asia, Australia and Europe
      Green states & provinces - EOS® implemented
    3. Soil & Groundwater Bioremediation Products Category Product Name Target Contaminants Biostimulation (Anaerobic) EOS ® EVO™ AquaBu pH ® VOS (under development) Chlorinated Solvents Perchlorate Chromate Explosives Radionuclides Acid Mine Drainage EAS™ Petroleum Hydrocarbons Biostimulation (Aerobic) EOx™ Petroleum Hydrocarbons Bioaugmentation BAC-9™ Chlorinated Solvents ENV-TCA20™ Chlorinated Alkanes PJKS-1™ Chlorinated Solvents
    4. Presentation Overview
      • What is EAS ™?
      • Why add sulfate?
      • What type of contaminates can be addressed?
      • Case Study
      • Conclusion
    5. What is EAS?
      • E lectron A cceptor S olution
      • A soluble product for anaerobic biodegradation of petroleum hydrocarbons
      • Delivers sulfate into the subsurface to:
        • Stimulate microbial growth for degradation of contaminants
    6. We Have A Petroleum Release
    7. Hydrocarbon Impacted Aquifers
    8. Conventional Wisdom
      • Add Oxygen
      • Electron Acceptors Products
      • Oxygen >>> Water, CO 2
      • Nitrate >>> Nitrogen, CO 2
      • Fe(III) >>> Fe(II), CO 2
      • Mn(IV) >>> Mn(II), CO 2
      • Sulfate >>> Sulfide, CO 2
      • CO 2 or acetic acid >>> Methane
      Contaminant (Electron donor) e.g. BTEX e - e - and C Energy Microbial Growth Aerobic Anaerobic
    9. Biodegradation of Fuel Contaminants In Groundwater Is Accomplished Mostly By Sulfate-Utilizing Microbes Based on median consumptions of electron acceptors at 38 hydrocarbon sites Ref: Weidemeier, T.H et al. All other electron accepting processes Based on median consumptions of electron acceptors at 74 sites – EPA-BP study Based on median consumptions of electron acceptors at 42 AFCEE sites
    10. Why Sulfate? Mass of Benzene Degraded per Unit Mass of EA: Oxygen = 0.33; Sulfate = 0.22 Electron Acceptor (EA) Maximum Concentration (mg/L) Potential Benzene Degraded (mg/L) Issues Oxygen (in air) 9 – 10 3.0 – 3.3
      • Limited solubility
      • Numerous oxygen sinks
      • Potential aquifer clogging
      • Biofouling near injection point
      Pure Oxygen 60 – 70 19.8 – 23.1 Sulfate 100 - 250 22.0 – 55.0
      • Hydrogen sulfide; never documented as an issue in the field
      • Secondary MCL for sulfate
        • 250 mg/L*
      EAS ™ >1,000 >220
    11. How Does EAS ™ Work?
      • Growth-Promoting Biological Reduction
      Energy + 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 - ] + + (Drawing Modified from AFCEE and Wiedemeier) Microbe Microbes EAS™
    12. 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.
    13. Why Sulfate Enhancement?
      • Accelerates site cleanup, typically in about 18 months
      • In Situ and minimally disruptive to the site and surroundings given injection can be accomplished in any well or geo-probe boring
      • Cost effective in achieving client remediation goals as most projects can be completed within 3-4 injections
      • Safe to the environment and people
      • A “Green Technology” which enhances natural conditions and reduces carbon foot print when compared to conventional remediation– a socially responsible approach to remediation
      • Proven by case study results on numerous site types
    14. Technical Advantages of EAS ™
      • Exists naturally
      • High solubility
      • Easily applied
      • Safe
      • Minimal site disruption
      • Minimal O&M
    15. Benefits
      • Minimal site disruption
        • In situ approach with no ongoing O&M activities
      • Cost effective
    16. Benefits
      • Safe
      • Green – Natural Process
    17. Benefits
      • Accelerated cleanup
        • Information gained significantly strengthens advocacy position with regulatory agencies
        • Monitoring frequency showed no lag time for acclimation of native sulfate reducing bacteria
    18. Contaminants that can be Treated with EAS ™
      • Petroleum Hydrocarbons
        • Aromatic Hydrocarbons
        • TPH
        • BTEX
        • MTBE
    19. How much EAS ™ is required
      • Generally 3-4 EAS ™ applications
      • ~ 0.11 - 0.33 lbs / CY
        • Depending on concentration levels
        • Site conditions
        • Etc.
    20. 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.
    21. Case Study Jackson, MI
      • Site Background
        • Former gasoline service station with two confirmed releases in 1992 and 2001.
        • Historical remedial efforts with limited success included groundwater pump and treat and monitored natural attenuation.
        • Geology consists of fine to medium sand with groundwater present about 10 feet bgs.
        • Site selected by MDEQ for Pilot Study to demonstrate feasibility of in situ EAS TM Technology.
        • Pilot study was not intended to be a “full scale” site remediation.
    22. Jackson, MI October 2007
      • Baseline Conditions
        • Sulfate is depleted in core
        • Sulfate background is > 50 ppm
        • Max. BTEX is >10,000 ppb
    23. Jackson, MI November 2006
      • 3 months after initial application
      • Sulfate still elevated in core of plume
      • BTEX >5,000 ppb is shrinking
    24. Jackson, MI April 2007
      • 6 months after first application
      • Sulfate concentrations have returned to baseline conditions
      • BTEX plume is stable with reduced peak concentrations
    25. Application Experience
      • Applied at over 100 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
      • Variety of geological and hydrogeological settings
    26. 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 sulfate-reducing microorganisms
    27. 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.
    28. Electron Acceptor Solution (EAS™) Sulfate Enhanced Anaerobic Bioremediation Contact: Craig Marlow 8248 Hidden Forest Drive Holland, Ohio 43528 Phone 419.867.8966 Fax 419.867.8976 Cell 419.349.7970 Email [email_address]
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