Technology Status Report: In Situ Flushing - CLU-IN
Technology Status Report: In Situ Flushing - CLU-IN
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