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Chlorinated Solvent Contamination

Chlorinated Solvent Contamination. Backyard Burning of Trash is now the #1 Dioxin Source!. Includes incineration of municipal solid waste, sewage sludge, and hazardous waste.

thomas-jordan
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Chlorinated Solvent Contamination

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  1. Chlorinated Solvent Contamination

  2. Backyard Burning of Trash is now the #1 Dioxin Source!

  3. Includes incineration of municipal solid waste, sewage sludge, and hazardous waste. • The US EPA will be issuing a new projection for dioxin emission from land-applied sewage sludge for 2002/2004 based on surveys to begin in Spring, 2001. The US EPA expects that the new projection will be lower than the value previously projected and here graphically displayed. • Other catagory includes: leaded and unleaded gasoline, land-applied 2,4-D, iron ore sintering, oil-fired utilities, EDC/vinyl chloride, lightweight aggregate kilns that combust hazardous waste, petroleum refined catalyst regeneration, cigarette smoke, boilers/industrial furnaces, crematoria, and drum reclamation.

  4. Approximately 400,000 sites of groundwater and soil in the U.S. are contaminated with chlorinated solvents. • The most common chlorinated solvents: • 1,2-dichloroetahne (1,2-DCA) • 1,1,1-trichloroethane (1,1,1-TCA) • carbon tetrachloride • methylene chloride, • chloroform • tetrachloroethene (PCE) • trichloroethene (TCE)

  5. Case study 1 • Methane enhance bioremediation and soil vapor extraction (Savannah River Site, S. Carolina) • DOE SRS facility generated nuclear textiles for defense operations for over twenty years. • TCE and PCE groundwater contamination in area of 300 square mile site.

  6. Approaches: horizontal wells were drilled and injected with 1% methane in air (Fig. 21-2).

  7. Sylvia et al., 1998

  8. The methane-air mixture as well as nutrients (N and P) were introduced to stimulate the growth of methanotrophs which produce the enzyme monooxygenase (MMO). Following the addition of methane, nutrients, and air, the population of MMO generating microorganisms increased to five times its original concentration after two months, then remained constant.

  9. The system was operated for 429 days. By the end of the demonstration, the concentration of TCE and PCE had been reduced to 2 mg/L. Note: PCE is not biodegraded aerobically. Most of the PCE was assumed to have volatilized and been captured in the vapor extraction well.

  10. It is estimated that air stripping without methane would require an estimated 10 years or more to achieve 95% removal of the contaminants, • whereas air stripping with methane would do this in less than 4 years with a savings of $1.5 million. • In fact, bioventing may be the only strategy that can lower TCE concentrations to meet drinking water standards of less than 5 ppb (mg/L).

  11. The horizontal wells improve methane and nutrient distribution which increases contact efficiency and helps reduce clogging potential. DOE received a patent for methane enhanced bioremediation (MEBR) technology in December, 1987.

  12. Case study 2 • Methane treatment technology (MTT) (rural Virginia) • MTT: Involves injecting air, methanes, and nutrients into the subsurface through injection wells to stimulate growth of methanotrophic bacteria. • Contaminants: TCE and PCE • Groundwater contaminant plume covers an area of about one acre, with the pH averaging between 5.4 and 6.6.

  13. Over 139 days of operation, methane levels detected in the vapor points declined to between 2 and 20 parts per million by volume (ppm V). • The most significant degradation occurred during the first three weeks of operation. • Results: • TCE from 2000 mg/L to 150 mg/L • PCE from 50 mg/L to nondetectable • This project demonstrated that TCE concentration can be significantly reduced within a short period of time (a few months).

  14. Case study 3 • Bioremediation of TCE through Toluene injection (Edwards air force base, california) • The chlorinated solvent contaminated site is approxi. 60 miles north of Los Angeles. • The site covers an area of 53 acres. • From 1958 to 1967, approx. 55 gallons of TCE was used each month to clean X-15 rocket plane • engines. • Concentrations of TCE in the groundwater plume varies between 500 and 1200 mg/L

  15. Wells were build with toluene as the primary substrate and oxygen were introduce by feeding. • Groundwater was pumped to the wells to be remediated, but never to the surface. • The system was operated for 410 days. • An area of 480 square meters was monitored by 14 monitoring wells.

  16. By day 284, the TCE removal efficiencies were 83% in the lower aquifer and 86% in the upper aquifer. • The system had an overall removal efficiency of 97.6%. TCE decreased from 1000 mg/L to 24 mg/L. • 99.98% of the toluene added to the system was removed within the first 2.5 m of travel from each of the treatment well. • Major disadvantage: Clogging of wells.

  17. Case study 4 • TCE contaminated ground water site along the Gulf Coast of Texas • Manufacture facility used TCE for 25 years around 1978 • Contaminated area: 420,000 square feet • Between 1986 to 1995, TCE decreased from 50 mg/L to 22 mg/L due to natural attenuation • A bioremediation treatment system was implemented to stimulate naturally occurring biological activity

  18. In situ full scale system was installed in the Summer of 1995 to increase anaerobic degradation rates. • Operation started Sept. 1995 with the addition of N and P only.

  19. Results: • An initial decrease in TCE concentration, but the degradation rate remained very slow. • In June of 1996, methanol was added to the system to serve as the primary substrate. • TCE concentrations: • June 1995: 2 to 88 mg/L • May 1996: 5.4 to 60 mg/L • Problem: the treatment area was not well mixed, it took about a year of operation to establish a well-mixed system

  20. Case study 5 • Anaerobic and aerobic biodegradation of PCE and TCE • Watertown Industrial site in Watertown, Massachusetts, including gas manufacturing plant, textile manufacturing, dry cleaning, and metal plating facilities. • Biodegradation of groundwater contaminants, first under anaerobic conditions then under aerobic conditions. • 1994, studies confirmed that natural attenuating is ongoing at the site.

  21. Groundwater is extracted from wells to the surface where nutrients, N, P and lactic acid are added. • The treatment remained anaerobic from Nov. 1996 to July 1997.

  22. Initial concentrations • PCE 1,300 mg/L • TCE 12,000 mg/L • Vinyl chloride 3,200 mg/L • After 8 months of anaerobic operation • PCE 1,000 mg/L • TCE 1,100 mg/L • Vinyl chloride 3,500 mg/L

  23. Conclusion: It did not work as well as expected • Solution: In July of 1997, The system was converted to operate under aerobic conditions in order to degrade TCE and it degradation intermediates. • This project is still on going at the time of the report

  24. Case study 6 • Anaerobic biodegradation of chlorinated solvents at Pinellas Science, technology, and Research (STAR) (Largo, FL) • From 1956 to 1994 (38 yrs), nuclear generators and components of r nuclear weapons were manufactured at the site. • Contaminants: TCE, DCE, VC, and methylene chloride. • Contaminant concentrations ranged from 10 to 400 mg/L in ground water, but one monitoring well exceeding 2900 mg/L/

  25. Contaminated area: 3-4 acres. • Electron donor used: • sodium benzoate • sodium lactate • methanol • Initial concentrations of the contaminants: • TCE: 46.6 mg/L • DCE: 45.6 mg/L • Methylene chloride: 19.2 mg/L • VC: 9.5 mg/L

  26. Most of the biodegradation took place in the first four to eight weeks. 90-95% of contaminants were removed from the system. • This was test in an area of 2,025 square feet and a full scale was planned to cleanup the entire groundwater plume which covers approx. 3.5 acres.

  27. Case study 7 • In-situ anaerobic bioremediation with bioaugmentation (Dover air force base, Delaware) • Contaminants: PCE, TCE, cis-DCE and VC. • Initial concentrations: • PCE: 50 mg/L • TCE: 5,000 TO 10,000 mg/L • cis-DCE: 1,000 TO 2,000 mg/L • VC: 20 mg/L

  28. The indigenous microorganisms were unable to further degrade DCE or VC • Microorganisms from the Pinellas STAR Center were cultured, then 370 liters were injected at a concentration of 108 cells per milliliter into the aquifer at the Dover site.

  29. Results • 99% of TCE and PCE were removed, both concentrations dropped below 5 ppm (b) • VC concentration dropped below 5 ppm, but not sure if it met the drinking water standard of 2 ppm (b) (5 ppm(b) is the detection limit) • The unit cost was $1,860 per 1000 gallons of groundwater treated ($1.86/gal)

  30. Case study 8 • Anaerobic biodegradation of CAHs (Eastern Pennsylvania) • Molasses was injected as a C/energy source for indigenous microorganisms. • The pump-and-treat system was operated for approx. 15 years (1982-1997) • In 1997, TCE concentration was about 100 ppb.

  31. Case study 9 • Anaerobic biodegradation of CAHs and chromium reduction at the Lycoming superfund site (Pennsylvania) • Contamination area: 28 acres • contaminants: • hexavalent chromium [Cr(VI)], 3 mg/L • cadmium (Cd), 0.8 mg/L • CAHs (TCE, DCE and VC). TCE up to 0.7 mg/L

  32. Molasses was injected as a C/energy source for indigenous microorganisms and to create reducing conditions in the subsurface so that microbial reduction can occur. • After 8 months treatment, • Cr (VI): from 2-3 mg/L to 0.5 mg/L in hot spot. 1.5 to 0.005 mg/L in other areas. • TCE; from 330 to 40 mg/L • DCE: from 670 to 180 mg/L • VC: from 20 mg/L to nondetectable.

  33. Additional areas of research in soil microbiology • Evaluation of suitable habitats, nutritional requirements, lag times, and degradation rates for various chlorinated contaminants • Optimization of environmental conditions, and stimulation of favorable growth conditions under site-specific variations. • Enhancing bioremediation in low permeability environments • Understanding bioaugmentation, including which organism degrade specific chlorinated compounds and how

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