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Annual report Chair on Drinking Water Engineering 2008 - TU Delft

Annual report Chair on Drinking Water Engineering 2008 - TU Delft

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Modeling of biological activated carb<strong>on</strong> filtrati<strong>on</strong><br />

Research objectives<br />

The research objective is to develop a quantitative simulati<strong>on</strong> model for biological activated (BAC) filtrati<strong>on</strong> in<br />

drinking water treatment. The model includes adsorpti<strong>on</strong> and biodegradati<strong>on</strong> processes and should be able to<br />

predict the removal of natural organic matter (NOM) and pesticides.<br />

Project outline<br />

Introducti<strong>on</strong><br />

Pre-oxidati<strong>on</strong> prior to granular activated carb<strong>on</strong> (GAC) filtrati<strong>on</strong> enhances biological activity, resulting in NOM<br />

removal. Oxidati<strong>on</strong> also reduces adsorbability of NOM. Both phenomena result in lower solid-phase c<strong>on</strong>centrati<strong>on</strong>s<br />

of NOM <strong>on</strong> activated carb<strong>on</strong>. The reduced solid-phase c<strong>on</strong>centrati<strong>on</strong>s causes less competiti<strong>on</strong> between<br />

pesticides and NOM, resulting in l<strong>on</strong>ger filter run times for pesticides.<br />

Approach<br />

Based <strong>on</strong> literature review a white box simulati<strong>on</strong> model for BAC filtrati<strong>on</strong> was developed. In an other work<br />

package of the project a biomass quantificati<strong>on</strong> method based <strong>on</strong> adeninotriphosphate (ATP) was developed<br />

and the dominant bacteria species in BAC filters were determined and characterized. Laboratory experiments<br />

were performed to determine the effect of oxidati<strong>on</strong> <strong>on</strong> the adsorpti<strong>on</strong> characteristics of the NOM. This provided<br />

data for model calibrati<strong>on</strong>. Pilot plant experiments for both ground and surface water were used for<br />

model validati<strong>on</strong>.<br />

Results<br />

Laboratory experiments showed that due to oxidati<strong>on</strong> and biodegradati<strong>on</strong> the solid-phase c<strong>on</strong>centrati<strong>on</strong>s of<br />

NOM reduce to 50% of the original values. Pesticide spiking experiments in a pilot plant at c<strong>on</strong>centrati<strong>on</strong>s of<br />

2 µg/l showed that BAC filter run times are up to two times l<strong>on</strong>ger than GAC filter run times (see figure 1). In<br />

the pilot plant biomass profiles were determined with the ATP <strong>on</strong> carb<strong>on</strong> method. Surprisingly ATP <strong>on</strong> carb<strong>on</strong><br />

c<strong>on</strong>centrati<strong>on</strong>s peak in spring and not in summer when temperatures are maximal.<br />

atrazine [µg C/l]<br />

2,5<br />

2<br />

1,5<br />

1<br />

TW-BAC1:<br />

0.7 g O3 ·g C<br />

influent<br />

0,5<br />

0<br />

EBCT 5 min<br />

EBCT 10 min<br />

EBCT 20 min<br />

0 100 200 300 400 500 600 700<br />

Time [days]<br />

Figure 1 - Atrazine breakthrough in GAC and BAC at empty bed c<strong>on</strong>tact times of 5 min and 10 min<br />

-1<br />

0-12 g H2O2 ·m-3 44 <str<strong>on</strong>g>Annual</str<strong>on</strong>g> <str<strong>on</strong>g>report</str<strong>on</strong>g> DWE <strong>2008</strong><br />

TW-GAC1:<br />

0 g O 3 ·m -3<br />

0 g H 2 O 2 ·m -3<br />

influent<br />

EBCT 5 min<br />

EBCT 10 min<br />

EBCT 20 min

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