Technology Status Report: In Situ Flushing - CLU-IN
Technology Status Report: In Situ Flushing - CLU-IN
Technology Status Report: In Situ Flushing - CLU-IN
Create successful ePaper yourself
Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.
<strong>In</strong> <strong>Situ</strong> <strong>Flushing</strong> Project Summaries<br />
GWRTAC Case Study Database<br />
GWRTAC ID: FLSH0060<br />
Project Name: National Water Res <strong>In</strong>st, Env Canada - Humic Acid <strong>Flushing</strong><br />
City: Burlington State/Province: ON<br />
Primary GWRTAC Personal<br />
Communication Source<br />
(Name/Organization):<br />
Project Summary:<br />
None<br />
None<br />
<strong>Report</strong>(s)/Publication(s) (GWRTAC Source):<br />
Lesage, et al., "Use of Humic Acids to Enhance the Removal of Aromatic Hydrocarbons from<br />
Contaminated Aquifers Part II: Pilot Scale"<br />
The following was excerpted from Lesage, et al., "Use of Humic Acides to Enhance the Removal of<br />
Aromatic Hydrocarbons from Contaminated Aquifers Part II: Pilot Scale":<br />
<strong>In</strong> this project, the aqueous solubility enhancement of aromatic hydrocarbons by humic acids was<br />
studied in laboratory columns (Xu et al, 1994) and in a large scale model aquifer (Lesage, et al.,).<br />
A petroleum source was placed into a constructed model aquifer with a very dense monitoring<br />
network. A humic acid (obtained as the sodium salt and prepared in solution) was used to flush the<br />
model aquifer. The purpose of the study was to determine whether humic acids could be used costeffectively<br />
to enhance dissolution and transport of aromatic hydrocarbons and provide an<br />
environmentally suitable alternative to artificial surfactants.<br />
The model aquifer tank was constructed of 1/4" industrial grade stainless steel (rectangular 2m x<br />
6m x 2m deep) with an external support structure made of steel beams. To induce water flow, a<br />
head tank separated from the aquifer material by a porous plate was used. The plate was<br />
constructed of 1/4" stainless steel, but perforated with 1" holes so as not to impede water flow. The<br />
sand aquifer material was retained by a polyester geotextile. To provide experimental control, the<br />
aquifer model was divided in half longitudinally using a series of stainless steel plates that were<br />
sealed and bolted together. The monitoring well network consisted of 72 bundles of 1/8" stainless<br />
steel tubes. Each bundle consisted of five sampling tubes terminating at 30 cm depth intervals.<br />
The bundles were spaced at 30 cm and 25 cm centres, parallel and perpendicular to the flow<br />
direction, respectively. Two withdrawal wells were installed, one on each side of the tank (5 cm ID,<br />
10 cm OD). A medium to coarse-grained sand (particle size range 75 um to 2.4 mm); hydraulic<br />
conductivity of 0.04 m/s) was used for the aquifer medium. Care was taken to prevent air<br />
entrapment and to remove residual chlorinated compounds during dry sand emplacement and<br />
subsequent tap water saturation, and the sand allowed to settle for a few weeks prior to conducting<br />
tracer experiments.<br />
A conservative tracer test was used to determine optimal placement of the petroleum source. The<br />
source was placed at a depth of 1.2 m, approximately 0.5 m downgradient from the head tank.<br />
Five additional monitoring well bundles were added along the center-line. The residual capacity of<br />
the sand was determined using a column experiment and it was found that approximately 500 mL<br />
of diesel fuel could be retained by 20 kg of sand. To emplace the source, 500 mL of diesel was<br />
Ground-Water Remediation Technologies Analysis Center<br />
Operated by Concurrent Technologies Corporation<br />
Appendix - Page 121 of 164<br />
Copyright GWRTAC 1998<br />
Revision 1<br />
Tuesday, November 17, 1998