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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 />

of 3 to 5 ft / day. The saturated zone was at a depth of less than 10 ft below the surface. The soil<br />

and groundwater at the site was found to be contaminated with low concentrations of a mixture of<br />

PCE, TCE, and weathered jet fuel (methylated alkanes). The compounds treated were PCE and<br />

aviation fuel at up to 1000 µg / kg and 1000 mg / kg, respectively. PCE in the ground-water was<br />

typically at 10 µg / L. The low concentrations were the result of previous remediations activities<br />

conducted at the site. Fluids were introduced to the target area via an upper well screen and<br />

recovered via a lower well screen located in the same casing. The innovative hydraulic system<br />

both injects a surfactant solution and extracts the ground-water/contaminant/surfactant fluid from a<br />

single borehole. Simultaneous injection to, and extraction from, a common vertical borehole<br />

creates a circulating flow pattern that can be used to capture mobilized contaminants that migrate<br />

vertically. <strong>In</strong> addition, a total of four monitoring wells (one upgradient, three downgradient) were<br />

installed. Each of the monitoring wells was screened over the top five feet of the saturated zone.<br />

Two piezometers were installed at different depths adjacent to the VCW. The shallow piezometer<br />

had a 2-foot screened section intercepting the seasonal water table; the deep piezometer has a 2foot<br />

screened section coinciding with the bottom 2 feet of the VCW. The demonstration area was<br />

10 feet by 10 feet and the depth to ground water is 15 feet. The Dow Chemical Co., a<br />

manufacturer of surfactants, has formed a partnership with the investigators to promote the<br />

development of this technology. The surfactant used was Dowfax 8390 at a delivered<br />

concentration of 36,000 mg/L (10 times the cmc value (3.8 wt%)). Dowfax 8390 has FDA approval<br />

for use as an indirect food additive. Prior to surfactant delivery a tracer test was performed using<br />

fluorescein and sodium chloride.<br />

The delivery/recovery sequence consisted of the following steps:<br />

<strong>In</strong>jection of 540 gallons of Dowfax 8390 Solution (36,000 mg/L) at a rate of 1 gpm,<br />

1 hour later, recovery of 40 gallons of surfactant/water solution,<br />

20 hours after surfactant delivery, freshwater cycling.<br />

It was found that due to the high hydraulic conductivity at the site, the extraction rate necessary to<br />

capture the surfactant and solubilized contaminants had to be about 10 to 15 times the injection<br />

rate. Produced fluids were analyzed at intervals to document surfactant mass removal. The<br />

analytical results showed that the surfactant increased the contaminant mass extracted by 40-fold<br />

and 90-fold for the PCE and jet fuel constituents, respectively. The surfactant solution<br />

demonstrated minimal sorption (retardation) and did not precipitate in the subsurface formation.<br />

Mass recovery for the surfactant solution exceeded 95 percent for the demonstration study. PCE<br />

concentration in the effluent was increased by more than two orders of magnitude (from 5 ug/L up<br />

to a high of 800 ug/L); LNAPL constituent concentrations were increased by more than an order of<br />

magnitude (from 10 mg/L up to 974 mg/L).<br />

A portion of the produced fluids were concentrated using micellar-enhanced ultrafiltration and then<br />

disposed of by a licensed contractor. The remainder of the effluent was sent to a carbon treatment<br />

system currently in operation at the site. At present, there are no known plans for further testing of<br />

surfactant systems at the Traverse City site.<br />

Researchers made the following recommendations as a result of this study (See Knox, et al., 1997<br />

for more detail).<br />

Ground-Water Remediation Technologies Analysis Center<br />

Operated by Concurrent Technologies Corporation<br />

Appendix - Page 104 of 164<br />

Copyright GWRTAC 1998<br />

Revision 1<br />

Tuesday, November 17, 1998

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