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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<strong>in</strong> one cycle ( 0, 36 and 66 m<strong>in</strong>utes) considered that the variation of the <strong>in</strong>fluent medium<br />
dur<strong>in</strong>g one hour should not be significant.<br />
3.3.2 Prolonged study, <strong>in</strong>termittent aeration<br />
A study of the effect of prolonged, <strong>in</strong>termittent aeration was made <strong>in</strong> order to observe<br />
how the <strong>N2O</strong> <strong>production</strong> was <strong>in</strong>fluenced by a longer anoxic period. Dur<strong>in</strong>g the first hour<br />
the reactor was operated <strong>in</strong> the same manner as above and the same sampl<strong>in</strong>g<br />
procedure was applied. The anoxic period of 20 m<strong>in</strong>utes dur<strong>in</strong>g a normal cycle was<br />
prolonged with 2 hours.<br />
Grab samples were taken <strong>in</strong> the effluent with 6 m<strong>in</strong>ute <strong>in</strong>tervals and every 36 m<strong>in</strong>utes <strong>in</strong><br />
the feed<strong>in</strong>g medium.<br />
3.3.3 Cont<strong>in</strong>uous aeration<br />
Measurements dur<strong>in</strong>g cont<strong>in</strong>uous aeration were performed at DO concentrations of<br />
~1.5 mg/l and ~1 mg/l. To determ<strong>in</strong>e the <strong>production</strong> of <strong>N2O</strong> gas dur<strong>in</strong>g these operation<br />
conditions the aeration was turned off and the unaerated period was determ<strong>in</strong>ed to 20<br />
m<strong>in</strong>utes to be comparable to the measurements done dur<strong>in</strong>g <strong>in</strong>termittent aeration.<br />
Measurements proceeded 20 m<strong>in</strong>utes after the aeration was switched on aga<strong>in</strong>.<br />
To exam<strong>in</strong>e if the accumulation of <strong>N2O</strong> gas <strong>in</strong> the water phase dur<strong>in</strong>g the anoxic period<br />
depended on <strong>in</strong>creased <strong>production</strong> or was an effect of stripp<strong>in</strong>g dur<strong>in</strong>g aeration, mix<strong>in</strong>g<br />
with pure N2 gas was used dur<strong>in</strong>g the anoxic period. The N2 gas flow was equal to the<br />
airflow dur<strong>in</strong>g the aerated period.<br />
Grab samples were taken <strong>in</strong> the effluent every 6 th m<strong>in</strong>ute and every 36 th m<strong>in</strong>ute <strong>in</strong> the<br />
<strong>in</strong>fluent medium.<br />
3.4 Calibration of microsensors<br />
The <strong>N2O</strong> <strong>production</strong> and NO2 − concentration profile were measured onl<strong>in</strong>e with Clarktype<br />
microelectrodes described <strong>in</strong> chapter 2.6. Before usage the microsensors were<br />
calibrated separately <strong>in</strong> a jacketed, temperature controlled beaker with 300 ml of pH<br />
regulated synthetic medium to assure the same sal<strong>in</strong>ity, temperature and pH of<br />
calibration solution and reactor, see Figure 11.<br />
The sensor to be calibrated was mounted <strong>in</strong> the calibration beaker, a stable sensor signal<br />
was awaited and the zero value was read and registered with Unisense’s software<br />
SensorTrace BASIC. A top mounted stirrer was used for fast mix<strong>in</strong>g and uniform<br />
concentration of the calibration solution.<br />
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