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N2O production in a single stage nitritation/anammox MBBR process

N2O production in a single stage nitritation/anammox MBBR process

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made the <strong>in</strong>crease <strong>in</strong> <strong>N2O</strong> accumulation will then be equal to the <strong>N2O</strong> <strong>production</strong> rate,<br />

(see appendix B for calculation example). The <strong>N2O</strong> <strong>production</strong> is calculated as % of<br />

removed <strong>in</strong>organic nitrogen. Two <strong>N2O</strong> <strong>production</strong> rates are estimated and referred to as<br />

<strong>in</strong>itial and maximum <strong>production</strong> rates. The <strong>in</strong>itial <strong>production</strong> rate is calculated from the<br />

<strong>in</strong>crease of <strong>N2O</strong> that can be seen <strong>in</strong> the water phase immediately after switch<strong>in</strong>g of<br />

aeration. Maximum <strong>N2O</strong> <strong>production</strong> is estimated between the two measur<strong>in</strong>g po<strong>in</strong>ts<br />

where the <strong>in</strong>crease <strong>in</strong> <strong>N2O</strong> has its maximum dur<strong>in</strong>g the unaerated period. Mean <strong>N2O</strong><br />

concentration <strong>in</strong> the water phase when the <strong>MBBR</strong> is aerated, calculated <strong>in</strong>itial and<br />

maximum <strong>N2O</strong> <strong>production</strong> rates, mean O2 concentrations dur<strong>in</strong>g the aerated period,<br />

mean nitrogen concentrations, reduction and removal rates for all measurements are<br />

summarised <strong>in</strong> Table 9 -Table 14. One figure of typical <strong>N2O</strong> and O2 profiles for each<br />

operation mode is shown <strong>in</strong> Figure 15 -Figure 20, <strong>N2O</strong> and O2 profiles for all<br />

measurements made are found <strong>in</strong> appendix C.<br />

4.3.2 Intermittent aeration.<br />

Measurements of produced <strong>N2O</strong> at <strong>in</strong>termittent aeration, (DO ~3.0 mg/l) were<br />

performed at four different occasions. Typical profiles of how <strong>N2O</strong> and DO changed<br />

dur<strong>in</strong>g the cycle are shown <strong>in</strong> Figure 15. The <strong>N2O</strong> concentration measured <strong>in</strong> the water<br />

phase varied with the aeration of the <strong>MBBR</strong>. When aeration started <strong>in</strong> the beg<strong>in</strong>n<strong>in</strong>g of<br />

the cycle the airflow striped <strong>N2O</strong> out of the water phase and the concentration decreased<br />

to a constant m<strong>in</strong>imum level. As soon as the aeration was shut off the <strong>N2O</strong> started to<br />

accumulate <strong>in</strong> the water phase until aeration was switched on aga<strong>in</strong> and the procedure<br />

started over as shown <strong>in</strong> Figure 15.<br />

N₂O (µmol/l)<br />

12<br />

10<br />

8<br />

6<br />

4<br />

2<br />

0<br />

4.5<br />

3.75<br />

2.25<br />

1.5<br />

0.75<br />

0<br />

0 20 40 60 80<br />

Time (m<strong>in</strong>)<br />

3<br />

DO (mg/l)<br />

N₂O<br />

(µmol/l)<br />

DO<br />

(mg/l)<br />

Figure 15. Concentration profiles of N 2O and O 2 dur<strong>in</strong>g a cycle of <strong>in</strong>termittent aeration, DO ~3 mg/l<br />

<strong>in</strong> the aerated phase. The cycle study started <strong>in</strong> the beg<strong>in</strong>n<strong>in</strong>g of the aerated period. N 2O gas was<br />

stripped from the water phase at the same time as the oxygen concentration rose.<br />

Initial <strong>N2O</strong> <strong>production</strong> varied between 5.6-11% of <strong>in</strong>fluent nitrogen concentration that<br />

was converted <strong>in</strong>to d<strong>in</strong>itrogen gas (here after referred to as removed <strong>in</strong>organic N-<br />

34

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