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Technology Status Report: In Situ Flushing - CLU-IN

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<strong>In</strong> <strong>Situ</strong> <strong>Flushing</strong> Project Summaries<br />

GWRTAC Case Study Database<br />

Phase 2 PreTest Waterflood (1.2 PV)<br />

Electrolyte flood (0.7 PV)<br />

<strong>In</strong>termediate Partitioning <strong>In</strong>terwell Tracer Test (2.9 PV)<br />

Phase 2 Chemical Delivery (PV 2.4)<br />

Phase 2 Water <strong>Flushing</strong> (PV 7.8)<br />

Final Partitioning <strong>In</strong>terwell Tracer Test (PV 4.3)<br />

Typical fluid delivery rates were on the order of 7.5 gpm, with flow split equally between the wells.<br />

Typical recovery rates were slightly higher, on the order of 9.2 gpm, and again flow was split<br />

equally between the wells. The water delivery rate to the hydraulic control well was approximately 7<br />

gpm.<br />

Fluids produced during the field demonstration were initially treated to approximately<br />

10 mg/L TCE by an existing onsite steam stripping unit. Fluids from this system were subsequently<br />

discharged to the AFB wastewater treatment system. This effort will develop data supporting the<br />

potential use of this technology for larger scale applications. <strong>In</strong> addition, researchers at the U.S.<br />

EPA Cincinnati Laboratory collected approximately 5,000 gallons of Phase II fluids to be used in<br />

testing of membrane filtration technologies for reuse of surfactant. This effort is funded by the U.S.<br />

Navy."<br />

Approximately 800 gallons of DNAPL was present in the test section of the aquifer. However,<br />

approximately 450 gallons of DNAPL was free-phase DNAPL and was removed by pumping prior<br />

to the first PITT. During the solubilization test, with an 8% surfactant injection over 0.6 days (0.6<br />

pore volumes), the TCE concentration in the central monitoring well rose from approximately 600<br />

mg / L prior to the injection to 40,000 mg / L after. The maximum DNAPL solubilization capacity<br />

was calculated to be 61,000 mg / L for this surfactant injection concentration. The concentrations<br />

in the 3 extraction wells were lower, likely due to dilution caused by streamtube convergence on<br />

these wells. Problems with surfactant foaming in the steam stripper occurred during this phase,<br />

which the investigators attempted to remedy in Phase II.<br />

The PITT indicated that there was a total of 346 gallons of residual DNAPL in the 4-ft thick test<br />

zone with an average residual DNAPL saturation of 20% (i.e., Sr = 0.20) or approximately 4%<br />

when measured over the whole, 20-ft thick, swept volume of the aquifer (i.e., Sr = 0.036). The<br />

solubilization test showed the selected surfactant to be extremely effective, and that there was no<br />

significant head loss due to mobilization of fines across the line-drive test zone. Furthermore, the<br />

steam stripper at OU2 readily treated the surfactant-rich waste waters.<br />

The results of the Phase I field operations were used to finalize the design of the Phase II<br />

surfactant flood. The Phase II flood, the purpose of which was to remove all remaining DNAPL<br />

from the test zone in the alluvium, was preceded and followed by PITTs so that the performance of<br />

the flood could be assessed. The surfactant flood consisted of the injection of a solution of 8%<br />

surfactant, 4% isopropyl alcohol and 0.7% NaCl, producing an interfacial tension of 0.02<br />

dynes/cm. The Phase II field operations lasted for 30 days, of which surfactant injection at 7.5<br />

Ground-Water Remediation Technologies Analysis Center<br />

Operated by Concurrent Technologies Corporation<br />

Appendix - Page 43 of 164<br />

Copyright GWRTAC 1998<br />

Revision 1<br />

Tuesday, November 17, 1998

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