NATO/CCMS Pilot Study Evaluation of Demonstrated and ... - CLU-IN
NATO/CCMS Pilot Study Evaluation of Demonstrated and ... - CLU-IN
NATO/CCMS Pilot Study Evaluation of Demonstrated and ... - CLU-IN
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<strong>NATO</strong>/<strong>CCMS</strong> <strong>Pilot</strong> Project on Contaminated L<strong>and</strong> <strong>and</strong> Groundwater (Phase III) January 2002<br />
Water samples collected on 11 days were tested for numerous parameters; on the whole, over 1,600<br />
individual results were obtained for water samples taken during pilot operation. The determined<br />
concentrations for dissolved organic carbons (DOC) ranged between 80 <strong>and</strong> 160 mg/l at the inlet. The<br />
DOC values correlate well with the CSB <strong>and</strong> TOC concentrations. No contaminant breakthrough was<br />
detected in samples from the outlets <strong>of</strong> the two columns over a period <strong>of</strong> almost half a year.<br />
The pilot tests with Columns 1 <strong>and</strong> 2 confirm that putting up an adsorbent wall is feasible.<br />
With respect to contaminant retention, results <strong>of</strong> the pilot tests indicate that the long-term effectiveness<br />
would be much higher than the estimated period <strong>of</strong> 30 years in the feasibility study.<br />
4. RESULTS AND EVALUATION<br />
The pilot tests confirm the findings <strong>of</strong> the feasibility study, to the effect that the site is suited to put up an<br />
adsorbent wall. The following statements can be made with respect to the present tests:<br />
The pilot tests show good contaminant retention in the activated carbon, in fact much higher than what<br />
was assessed in the feasibility study. Contaminant breakthrough for toluene <strong>and</strong> trichloroethylene was<br />
determined at sampling point S2P50 (i.e., after flow through 50 cm), Column 2, only at the end <strong>of</strong> the 5month<br />
pilot test operation. By this time, throughput had reached 600 times the bed volume.<br />
The pilot tests indicate that the durability <strong>of</strong> the wall given a 70 cm-thick activated carbon layer would be<br />
much higher than the 30 years estimated in the feasibility study. The thickness <strong>of</strong> the carbon layer should<br />
therefore be reduced when the wall is put up.<br />
The DOC concentrations established during the pilot tests can almost entirely be traced to the<br />
contaminants detected at the site. It is therefore to be expected that the adsorbing potential <strong>of</strong> the activated<br />
carbon will not be impaired by natural organic compounds, such as human.<br />
Data pertaining to the contaminant breakthrough suggest that the depletion <strong>of</strong> the adsorbing capacity <strong>of</strong><br />
the activated carbon is accompanied by a sharp peak in the concentration <strong>of</strong> volatile substances. A<br />
suitable monitoring system should therefore be set up when the adsorbent wall is erected.<br />
The fact that the activated carbon could be regenerated after disassembling the plant suggests economic<br />
operation <strong>of</strong> the adsorbent wall.<br />
Laboratory analyses <strong>of</strong> the water <strong>and</strong> activated carbon samples indicate that iron <strong>and</strong> manganese<br />
precipitation will be insignificant <strong>and</strong> will not block the adsorbent wall.<br />
Microbial activity could not be detected in the gravel filter or in the activated carbon; it may be concluded<br />
that under the given site conditions, the build-up <strong>of</strong> bacterial film does not pose a risk.<br />
Preliminary laboratory tests to determine the choice <strong>of</strong> activated carbon as well as pilot tests must be<br />
carried out in all cases prior to setting up an adsorbent wall given the variance in site conditions.<br />
5. COSTS<br />
The costs for conducting the field tests have been EURO 50.000,--. The overall costs to erect the wall<br />
system <strong>and</strong> then fill it with activated carbon are estimated to be EURO 750.000,--. Included are additional<br />
costs for monitoring the water quality for 30 years, which is as long as the minimum performance time <strong>of</strong><br />
one single filling will be.<br />
In comparison with traditional pump-<strong>and</strong>-treat groundwater remediation costs, the proposed permeable<br />
reactive barrier system will be at least 25% less expensive.<br />
6. REFERENCE<br />
Eberhard Beitinger <strong>and</strong> Eckart Bütow. Machbarkeitsstudie zum Einsatz einer Adsorberw<strong>and</strong> -<br />
”Schönebecker Schlucht” in Essen, Internal Report, WCI, Wennigsen, 1997 (not published)<br />
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