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1 Combined Perchlorate and RDX Treatment in Biological Fluid Bed Reactors PRESENTATION AT THE NDIA 30 TH ENVIRONMENTAL AND ENERGY SYMPOSIUM APRIL 7, 2004.

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Presentation on theme: "1 Combined Perchlorate and RDX Treatment in Biological Fluid Bed Reactors PRESENTATION AT THE NDIA 30 TH ENVIRONMENTAL AND ENERGY SYMPOSIUM APRIL 7, 2004."— Presentation transcript:

1 1 Combined Perchlorate and RDX Treatment in Biological Fluid Bed Reactors PRESENTATION AT THE NDIA 30 TH ENVIRONMENTAL AND ENERGY SYMPOSIUM APRIL 7, 2004 Presented by William J. Guarini

2 2 Acknowledgements Aerojet U.S. Army U.S. Army Corps of Engineers U.S. Navy US Filter SERDP ESTCP AMEC

3 3 Presentation Overview Biodegradation of Perchlorate/RDX/MNX Fluidized Bed Reactor Case Histories – Full Scale FBR -Aerojet -Longhorn MMR Demo – Perchlorate/RDX/MNX Summary

4 4 Perchlorate Biodegradation Cl - + H 2 O Biomass + CO 2 Substrate ClO 4 - ClO 3 - ClO 2 - * Highly Favorable Reaction (-801 kJ/mol acetate) * Several Different Genera Isolated (Wolinella, Ideonella, Dechlorospirillum, Dechlorisoma)

5 5 Chemical Structures Hexahydro-1,3,5-trinitro-1,3,5-triazine (RDX) 2,4,6-Trinitrotoluene (TNT) Octahydro-1,3,5,7-tetranitro- 1,3,5,7-tetrazocine (HMX)

6 6 Generalized Biodegradadtion In most cases, transformation and/or biodegradation appears to be a gratuitous activity, often times “cometabolic” in nature. Ability to transform explosives seems to be widespread, and has been observed in:  bacteria (both Gram+ and Gram- genera)  fungi (mostly white rot species)  Plants Most commonly observed mechanism is sequential reduction of the NO 2 - groups, followed by eventual ring cleavage.

7 7 Generalized Biodegradation Pathways RDX Hexahydro-1-nitroso- 3,5-dinitro- 1,3,5-triazine (MNX) DNXTNX Formaldehyde Methanol Hydrazine CO 2 N 2 O Methylenedinitramine Bis(hydroxymethyl) nitramine

8 8 Utilization of Electron Acceptors

9 9 FLUIDIZED BED REACTOR EFFLUENT FEED CONTAMINATED GROUNDWATER NUTRIENT(S) ELECTRON DONOR INFLUENT RECYCLE Distribution Headers Biomass Control Fluidized Bed Reactor Flow Schematic

10 10 Fluidization of Media FBR Post Start-up 25-30% FBR Set Specific Density of Sand Particles As the Biomass Grows, the Specific Density Decreases as Combined Volume of the GAC and Biomass Increases Microbes 40-60% Start-up

11 11 FBR Advantages High biomass concentration means long SRT and short HRT High volumetric efficiency translates to compact system; Simplicity of operation minimizes need for operator attention

12 12 Key Mechanical Components Device and method used to distribute influent flow to the reactor Device and method used to control the expansion of the fluidized bed due to biofilm growth Method to control electron donor dosage rate

13 13 FBR SYSTEM –2 - 8 mg/L perchlorate –6,000 GPM flow rate –Four 14-ft diameter units –Ethanol as electron donor –GAC media Aerojet Facility - Rancho Cordova California Full-Scale Perchlorate Treatment System Atlas V

14 14 Aerojet

15 15 Aerojet FBR Performance Start-up data shown: 5 years

16 16 Full-Scale FBR System #2 Longhorn Army Ammunition Plant – Karnack, Texas FBR System –15 mg/L perchlorate design –50 gallons per minute flow rate –One 5-ft diameter unit –Acetic acid as electron donor –GAC media

17 17

18 18

19 19 Longhorn

20 20 LHAAP FBR Performance InfluentEffluent Currently operating 3+ years. Effluent consistently <4 µg/L.

21 21 Other FBR Sites McGregor NWIRP Kerr-McGee Chemical, LLC Jet Propulsion Lab

22 22 MMR FBR Site Evaluation Can FBR systems remediate low concentrations of perchlorate? –Less than 100  g/L (ppb) Can FBR systems concurrently degrade explosives as well as perchlorate? –Both biological processes are anoxic reductive processes requiring electron donors Can a single FBR replace traditional lead-lag arrangement of FBR and GAC? What treatment levels are attainable?

23 23 MMR Groundwater Contaminant Concentrations Perchlorate 100  g/L RDX190  g/L HMX20  g/L Nitrate8 mg/L

24 24 FBR Treatability Study - Set-up Granular activated carbon (GAC) FBR #1 fed acetate (simple organic substrate) FBR #2 fed molasses (complex organic substrate) FBR #3 was a control (no substrate or nutrients) Each column fed groundwater until perchlorate effluent concentrations approached influent concentrations meaning GAC saturated with perchlorate Each column wrapped with cooling coil to maintain temperature at ~17  C

25 25 FBR Treatabililty Results - Perchlorate

26 26 FBR Treatability Results - RDX

27 27 RDX Mass Balance

28 28 RDX Intermediates and Other Explosives

29 29 FBR Treatability Study Conclusions Success with FBR utilizing acetate and electron donor substrate (FBR #1) At HRT of 80 minutes –Perchlorate reduced from 100  g/L to < 1.5  g/L –RDX reduced from 190  g/L to < 2  g/L HRT of 35 minutes –Perchlorate reduced from 100  g/L to < 1.5  g/L –RDX could be removed by secondary GAC unit

30 30 FBR Treatability Study Conclusions The molasses fed FBR (FBR #2) degraded perchlorate and RDX, but to a lesser extent RDX that sorbed to the GAC in FBR #1 (acetate) was consistently 2 orders of magnitude lower than in FBR #2 and FBR #3 (control). This tells us that the biologically active film on the GAC in FBR #1 was effective at destroying a significant amount of sorbed RDX FBR can perform as a stand alone alternative to traditional lead-lag multiple step treatment trains for perchlorate and explosives


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