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Technology Status Report: In Situ Flushing - CLU-IN

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Table 4 <strong>In</strong> <strong>Situ</strong> <strong>Flushing</strong> - Recovered Contaminant Mass / Economic <strong>In</strong>formation Available<br />

Total Number of Case Studies = 84<br />

GWRTAC Project <strong>Report</strong>ed Contaminant <strong>Report</strong>ed Fraction of Economic Scale of<br />

ID Name Mass Recovered <strong>In</strong>ital Mass Recovered <strong>In</strong>formation Project<br />

FLSH0015 Hill Air Force Base, UT (Cell 3,<br />

OU1 - Cosolvent Mobilization)<br />

FLSH0016 Hill Air Force Base, UT (Cell 5,<br />

OU1 - Surfactant Mobilization)<br />

FLSH0017 Hill Air Force Base, UT (Cell 6,<br />

OU1 - Surfactant Solubilization)<br />

FLSH0018 Hill Air Force Base, UT (Cell 8,<br />

OU1 - Surfactant/Cosolvent<br />

Solubilization)<br />

FLSH0019 Hill Air Force Base, UT (OU2 -<br />

Micellar Flood)<br />

FLSH0022 Hill Air Force Base, UT (Test1,<br />

OU1 - Cosolvent Solubilization)<br />

FLSH0023 Hooker Chemical/Ruco Polymer,<br />

NY<br />

FLSH0024 Howard University, Washington,<br />

DC - Treatment of PCBs with<br />

Surfactants<br />

80% Total NAPL Content Removed from Test<br />

Cell (>90% of More Soluble Contaminants<br />

and 70-80% of Less Soluble Compounds<br />

Approximately 350 L (92 gallons) 72% NAPL (Based on Tracer Test), 64-96%<br />

(Based on Core Estimates), 62-82% (Based<br />

on Mass Balance)<br />

Pilot/Field<br />

Demonstration<br />

Pilot/Field<br />

Demonstration<br />

Pilot/Field<br />

Demonstration<br />

Pilot/Field<br />

Demonstration<br />

341 Gallons, Based on PITT 99% Thus, over the course of a few months, at a Pilot/Field<br />

cost of about $3,000/gallon, 98.5% of the<br />

residual DNAPL was removed. This can be<br />

compared with the original USAF estimate for<br />

cleanup of the DNAPL that used the<br />

traditional time frame of 30 years with a cost o<br />

Demonstration<br />

Approximately 350 L (92 Gallons) NAPL >85% Cell-Wide Basis, >95% in Central<br />

Flood Zone, >75% in Bottom 0.5 m<br />

Pilot/Field<br />

Demonstration<br />

Project not yet Begun Project not yet Begun Full-<br />

Scale/Commercial<br />

Project is in Progress Project is in Progress Laboratory/Bench<br />

Scale<br />

FLSH0025 JADCO-Hughes, Belmont, NC Project not yet Begun Project not yet Begun Pilot/Field<br />

Demonstration<br />

FLSH0001 Koppers Co. <strong>In</strong>c., Seaboard<br />

Plant, Kearny, NJ<br />

FLSH0026 Laramie, WY, Private wood<br />

treating site<br />

Project is in Progress; During First 3 Months<br />

of Operation, Over 11,000 Gallons DNAPL<br />

Collected<br />

1,900 Gallons PAH-Contaminated Oil<br />

Removed from 27x27' Test Cell; 23,600<br />

Gallons Oil were Produced from 130x130'<br />

Test Cell<br />

FLSH0027 Lee Chemical, Liberty, MO Project is in Progress; Performance Results<br />

not yet Available<br />

FLSH0028 Lipari Landfill, Pitman, NJ Project is in Progress; Performance Results<br />

not yet Available<br />

Ground-Water Remediation Technologies Analysis Center<br />

Operated by CTC 1-800-373-1973 Page 22<br />

Project is in Progress Pilot/Field<br />

Demonstration<br />

94% Reduction in Oil Concentration (27x27'<br />

Test Cell)<br />

Project is in Progress; Performance Results<br />

not yet Available<br />

Project is in Progress; Performance Results<br />

not yet Available<br />

Full-scale applications of the chemically<br />

enhanced recovery technique would require<br />

an extensive piping network and large<br />

amounts of fluids and chemicals. Based on<br />

extrapolation from the 1989 pilot test, fullscale<br />

in situ soil flushing would require more<br />

Pilot/Field<br />

Demonstration<br />

Full-<br />

Scale/Commercial<br />

Full-<br />

Scale/Commercial<br />

GWRTAC 1998<br />

As of 11/17/98

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