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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<strong>In</strong> <strong>Situ</strong> <strong>Flushing</strong> Project Summaries<br />
GWRTAC Case Study Database<br />
2,500 gallons per cell. The hydraulic conductivity of the saturated potion of the upper sand and<br />
gravel unit at OU1 is 10-1 to 10-2 cm/sec based on aquifer test data, and 10-2 to 10-5 cm/sec<br />
based on slug test data. For all of the flushing experiments (those with surfactants, cosolvents,<br />
and cyclodexdrin), the flushing rate will be approximately one pore volume per day. Prior to and<br />
after treatment of each cell, a partitioning tracer test has or will be performed. The mix of tracers<br />
will be designed according to the expected volume of NAPL within the cell before and after<br />
treatment. Among the tracers, hexanol and dimethylpentanol may be included.<br />
For the test at Cell 3, OU 1, tert-butanol mixed with n-hexanol was used as the flushing solution.<br />
The 3 m x 5 m test cell contains approximately 1,500 gallons of water (i.e., the PV). A partitioning<br />
tracer test was performed on the cell with bromide, ethanol, methanol, tert-butanol, methylhexanol,<br />
and dimethyl pentanol as tracers. From this test, the estimated amount of NAPL in the<br />
cell is 60 gal. The LNAPL originated from petroleum hydrocarbons and spent solvents, and is a<br />
complex mixture of aromatic and aliphatic hydrocarbons, chlorinated solvents, and other<br />
compounds. The bulk of the NAPL composition consists of low solubility, low vapor pressure<br />
compounds, and the NAPL not soluble in pure methanol, ethanol, acetone, or isopropanol.<br />
The test involved the injection and extraction of 7,000 gallons of a mixture of tert-butanol and nhexanol.<br />
Specifically, the following chemical system was delivered in sequence:<br />
0.85 pore volume of 95 vol% tert-butanol/hexanol (1 pore volume is approximately 1,500 gal)<br />
1.33 pore volumes of 81 vol% tert-butanol/hexanol, 16 vol% n-hexanol<br />
2.33 pore volumes of 95 vol% tert-butanol<br />
0.33 pore volume of 47.5 vol% tert-butanol<br />
30 pore volumes of waterflood<br />
It was anticipated that most of the NAPL will be removed before the total volume of alcohol is<br />
pumped. The earlier cosolvent test at Hill AFB performed by The University of Florida group (Test<br />
1, Operational Unit 1) was designed to solubilize the NAPL. The intent in this test is to mobilize the<br />
NAPL to basically remove it in a plug. Formulating a cosolvent mixture that will mobilize this<br />
specific complex NAPL has required extensive laboratory work. Fluids produced during the effort<br />
were stored on site with plans for eventual discharge to the onsite wastewater treatment plant.<br />
The results of post flood soil coring indicate better than 90% removal of the more soluble<br />
contaminants (TCA, toluene, ethylbenzene, xylenes, trimethylbenzene, naphthalene) and 70% to<br />
80% removal of less soluble compounds such as decane and undecane. The results of pre-flood<br />
and post-flood NAPL partitioning tracer tests show about 80% removal of the total NAPL content<br />
from the test cell.<br />
<strong>Report</strong>(s)/Publication(s) (Additional <strong>In</strong>formation Sources):<br />
Falta, et. al., 1997: Abstract "Field Evaluation of Cosolvent-Enhanced <strong>In</strong>-<strong>Situ</strong> Remediation",<br />
CRADA CR-821992-01-0 between R.S. Kerr Environmental Research Lab and Clemson University,<br />
July 28, 1997.<br />
Ground-Water Remediation Technologies Analysis Center<br />
Operated by Concurrent Technologies Corporation<br />
Appendix - Page 30 of 164<br />
Copyright GWRTAC 1998<br />
Revision 1<br />
Tuesday, November 17, 1998