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UV/H2O2 Treatment an Essential Barrier in a - PWN Technologies

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degradation [%]<br />

100<br />

80<br />

60<br />

40<br />

20<br />

0<br />

0 0.2 0.4 0.6 0.8 1<br />

energy <strong>in</strong>put [kWh/m 3 ]<br />

© Bram J. Martijn, Peer C. Kamp, Joop C. Kruithof<br />

4 mg/L <strong>H2O2</strong><br />

8 mg/L <strong>H2O2</strong><br />

15 mg/L <strong>H2O2</strong><br />

25 mg/L <strong>H2O2</strong><br />

Figure 2: Atraz<strong>in</strong>e degradation for several process conditions, bench scale experiments <strong>in</strong> pre-treated IJssel Lake<br />

water<br />

Depend<strong>an</strong>t on the chemical characteristics of the pollut<strong>an</strong>t, either photolysis or hydroxyl radical oxidation plays a<br />

pre-dom<strong>in</strong><strong>an</strong>t role. Figure 3 illustrates this for the degradation of NDMA, primarily due to photolysis, 1,4-diox<strong>an</strong>e,<br />

completely based on hydroxyl radical oxidation <strong>an</strong>d atraz<strong>in</strong>e degradation, based on a comb<strong>in</strong>ation of both.<br />

degradation<br />

[%]<br />

120<br />

100<br />

80<br />

60<br />

40<br />

20<br />

0<br />

<strong>UV</strong>/<strong>H2O2</strong>-oxidation <strong>UV</strong>-photolysis<br />

NDMA atraz<strong>in</strong>e 1,4-diox<strong>an</strong>e<br />

Figure 3: Ratio of degradation by oxidation <strong>an</strong>d photolysis for NDMA, atraz<strong>in</strong>e <strong>an</strong>d 1,4-diox<strong>an</strong>e<br />

Pilot scale research <strong>UV</strong>/<strong>H2O2</strong> phase 1<br />

Research was extended to pilot scale. Figure 4 presents the atraz<strong>in</strong>e degradation for several hydrogen peroxide<br />

dosages for both the bench scale <strong>an</strong>d the pilot scale <strong>in</strong>stallation. A slight decrease <strong>in</strong> efficiency c<strong>an</strong> be observed,<br />

mov<strong>in</strong>g from bench scale to pilot scale.

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