1 In Situ Oxidation of PAH Contaminants Associated With Former Manufactured Gas Plants Ron Jensen Southern California Edison 1.

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Presentation transcript:

1 In Situ Oxidation of PAH Contaminants Associated With Former Manufactured Gas Plants Ron Jensen Southern California Edison 1

2 Santa Barbara MGP Site

3

4 Historical Museum Main museum completed in 1965 –Adobes made from onsite soil Courtyard used for public gatherings Two historic adobes dating to schools adjacent to site

5 Area of Contamination Highest contaminant levels

6 Gas Holder Excavation Excavated gas holder below parking lot –Source of groundwater contamination –Portion of holder base under museum wing –Vertical excavation next to buildings Removed 1,500 cubic yards of soil to 15 foot depth

7 In-situ Ozone Sparging 27 Ozone sparge wells 11 Air sparge wells 34 Vapor extraction wells Rationale –Cannot disrupt current land use –Dewatering and excavation not feasible because of historic structures

8 Treatment Zone Summary 27,000 cubic yards of soil treated by ozone sparging 10,000 cubic yards of soil treated by air sparging Treatment area = 65,000 square feet Depth to groundwater feet below ground surface Thickness of treatment zone feet

9

10

11 Treatment Compound Interior Secures equipment Self-enclosed trailers –Oxygen generation –Ozone generation –Vapor extraction Trailers customized to attenuate sound Two 2,000-pound carbon vessels Ozone destruct catalyst vessel Single permitted emission point from Air District Low-impact electric cart for well sampling and maintenance

12 Treatment Compound - Exterior Wall is consistent with architecture of museum Wall mitigates visual impacts Designed to attenuate noise to 60 decibels at property line Sliding gate allows easy access to interior of compound

13 Oxygen Generation Trailer Produces oxygen feedstock for ozone generator Liquid oxygen - too risky Duplicate vessels containing a molecular sieve (zeolite) remove nitrogen from ambient air

14 Oxygen Generation Trailer 90% pure oxygen stored in steel pressure vessel at psi for ozone production Oxygen volume produced is 500 cubic feet per hour (12,000 cubic feet per day) System shuts off if oxygen levels exceed 25% inside trailer

15 Ozone Generation Trailer Ozone generator produces 50 pounds per day Final gas stream comprised of 6% ozone and 92% oxygen Generator operates at 15 psi at 8 cubic feet per minute

16 Ozone Generation Trailer Produced gas is boosted to 45 psi by 2-stage oiless compressor Up to four valves can be activated at a time to distribute produced gas to wells Well pressures vary from psi depending on tightness of formation

17 Ozone Generation Trailer Ozone generator shuts down if ozone concentration inside trailer exceeds 300 ppb (alerts at 100 ppb) Each ozone injection well has dedicated 3/4-inch Teflon tube connecting manifold valve to sparge well

18 Soil Vapor Extraction Moisture knockout vessel receives influent vapor Designed to operate at 400 cubic feet per minute Vapor concentration averaged 175 ppmv (as hexane) total reactive organic compounds upon startup. Concentrations decreased by 60% within 3 weeks of start up. SVE/air sparge only for first 30 days of treatment regime

19 Ozone Distribution 20,000 lineal feet of 3/4-inch teflon tubing All piping and tubing located below ground in PVC conduits Some wells have nested sparge points on 10 foot vertical increments Depths of sparge points vary from 30 to 55 feet below ground surface

20 Ozone Distribution Wire-wrapped sparge screens (0.030 inch slots) are 30 inches long and made of 304 stainless steel Well vault lids coated with urethane glue and impregnated with decomposed granite Ozone monitors contained in piping distribution vault Ozone monitoring points positioned at 5 and 12 feet below surface around museum basement

21 Ozone Monitoring and Control Continuous VES operation PLC shuts off ozone injection if: –Museum HVAC turns off –Museum monitors detect 100 ppb ozone –Power failure –VES shuts down Initially tested system with Helium Additional vapor wells near museum and screened below basement

22 Cleanup Goals Groundwater –Benzo(a)pyrene: 0.2 ppb –Benzene: 1.0 ppb –Naphthalene: 21 ppb –TPH: 1.0 ppm Soil –Reduce contaminants to protect groundwater –Leaching tests used to assess acceptable endpoint to protect groundwater

23 Contingent Remedial Strategy Ozone treatment scheduled for two years: July 2002 through June 2004 In the event MCLs for groundwater are not met within allocated time frame, strategy will switch to monitored natural attenuation Land use covenant will be required to address residual deep soil contamination