N2O production in a single stage nitritation/anammox MBBR process
N2O production in a single stage nitritation/anammox MBBR process
N2O production in a single stage nitritation/anammox MBBR process
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12<br />
10<br />
4.5<br />
3.75<br />
N₂O (µmol/l)<br />
8<br />
6<br />
4<br />
2<br />
3<br />
2.25<br />
1.5<br />
0.75<br />
DO (mg/l)<br />
N₂O<br />
(µmol/l)<br />
DO<br />
(mg/l)<br />
0<br />
0<br />
0 50 100 150 200<br />
Time (m<strong>in</strong>)<br />
Figure 3. Concentration profiles of N 2O and O 2 dur<strong>in</strong>g prolonged unaerated period.<br />
At first the <strong>N2O</strong> accumulation is rather l<strong>in</strong>ear, when DO decreases under 1 mg/l the<br />
accumulation rate of <strong>N2O</strong> is reduced until a maximum concentration is reached at DO<br />
concentrations close to 0 mg/l. The <strong>N2O</strong> concentration is constant under a period of 20-<br />
50 m<strong>in</strong>utes and then slowly starts to decrease as seen <strong>in</strong> Figure 3.<br />
Cont<strong>in</strong>uous aeration<br />
Measurements with cont<strong>in</strong>uous aeration were performed at DO concentrations of ~1.5<br />
mg/l and ~1 mg/l. To be able to determ<strong>in</strong>e the <strong>production</strong> of <strong>N2O</strong> gas dur<strong>in</strong>g these<br />
operation conditions the aeration was turned off. The unaerated period was chosen to<br />
20 m<strong>in</strong>utes to be comparable with the measurements done dur<strong>in</strong>g <strong>in</strong>termittent aeration.<br />
Measurement proceeded 20 m<strong>in</strong>utes after the aeration was switched on aga<strong>in</strong>. Two<br />
measurements were performed at a constant aeration with a DO concentration of ~1.5<br />
mg/l and ~1 mg/l respectively a typical profile of O2 and <strong>N2O</strong> concentrations are shown<br />
<strong>in</strong> Figure 4.<br />
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