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ΕΘΝΙΚΟ ΜΕΤΣΟΒΙΟ ΠΟΛΥΤΕΧΝΕΙΟ

ΕΘΝΙΚΟ ΜΕΤΣΟΒΙΟ ΠΟΛΥΤΕΧΝΕΙΟ

ΕΘΝΙΚΟ ΜΕΤΣΟΒΙΟ ΠΟΛΥΤΕΧΝΕΙΟ

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Conclusions<br />

The pilot-scale GAC column system was found to effectively remove all of the<br />

ECs examined already from the first batch experiment. In the second batch<br />

experiment, despite the problems arisen, this removal started to be quantified (the<br />

breakthrough limits for each EC were established and the first constants N0 and K, as<br />

well as the first values of Lcritical were calculated, although these results are not<br />

trustworthy).<br />

The third and fourth batch experiments gave much more clear results<br />

(especially the third batch experiment) about the breakthrough of each EC, compared<br />

to the second batch experiment. However, probably because of the microbiological<br />

activity observed (especially in the fourth batch experiment) the values of the<br />

constants N0 and K do not change as usual versus the linear flow rate.<br />

As for the ECs examined, in every batch experiment it seems that the EDCs<br />

examined (and particularly Triclosan) were more effectively removed from the water<br />

compared to the PPCPs (that’s why in the EDCs lower breakthrough limits were<br />

established). Among the PPCPs no significant differences were observed in their<br />

removal from the water.<br />

In conclusion, for a proper design of a GAC column unit in a water treatment<br />

plant a design diagram with the values of N0 and K versus the linear flow rate is<br />

required. Therefore it is necessary additional batch experiments to be conducted in<br />

different linear flow rates, so that this design diagram for each EC to be completed.<br />

Furthermore, due to the fact that microbiological activity was observed in<br />

every batch experiment it would be better during the design of the GAC column unit<br />

to include that microbiological activity, as it seems to help in the removal of those<br />

substances (particularly in the fourth batch experiment).<br />

Finally, due to the fact that one of the main entrance route of EDCs and PPCPs<br />

in the aquatic environment is through the effluents of wastewater treatment plants it is<br />

necessary to also investigate the potential of the removal of those substances from the<br />

effluents of wastewater treatment plants. In case of the effluents a much smaller GAC<br />

column service time and a much faster breakthrough limit reach is expected,<br />

compared to those found in the water samples of this thesis, because of the presence<br />

of Natural Organic Matter (NOM) in the effluents.<br />

~ xiii ~

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